EP1748269B1 - Rotary furnace for manufacturing activated carbon - Google Patents
Rotary furnace for manufacturing activated carbon Download PDFInfo
- Publication number
- EP1748269B1 EP1748269B1 EP06013903A EP06013903A EP1748269B1 EP 1748269 B1 EP1748269 B1 EP 1748269B1 EP 06013903 A EP06013903 A EP 06013903A EP 06013903 A EP06013903 A EP 06013903A EP 1748269 B1 EP1748269 B1 EP 1748269B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- rotary tube
- reinforcing element
- rotary
- activated carbon
- mixing elements
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims description 96
- 238000004519 manufacturing process Methods 0.000 title claims description 33
- 230000003014 reinforcing effect Effects 0.000 claims description 107
- 238000002156 mixing Methods 0.000 claims description 64
- 238000003466 welding Methods 0.000 claims description 39
- 239000000463 material Substances 0.000 claims description 30
- 229910000831 Steel Inorganic materials 0.000 claims description 19
- 230000004913 activation Effects 0.000 claims description 19
- 239000010959 steel Substances 0.000 claims description 19
- 229910052799 carbon Inorganic materials 0.000 claims description 14
- 230000000087 stabilizing effect Effects 0.000 claims description 4
- 238000013019 agitation Methods 0.000 claims 1
- 238000003763 carbonization Methods 0.000 description 11
- 238000005260 corrosion Methods 0.000 description 10
- 230000007797 corrosion Effects 0.000 description 10
- 239000007789 gas Substances 0.000 description 8
- 239000003245 coal Substances 0.000 description 7
- 239000003456 ion exchange resin Substances 0.000 description 7
- 229920003303 ion-exchange polymer Polymers 0.000 description 7
- 229920000642 polymer Polymers 0.000 description 7
- 239000007858 starting material Substances 0.000 description 7
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical class C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 230000001590 oxidative effect Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 238000004886 process control Methods 0.000 description 6
- 230000006641 stabilisation Effects 0.000 description 6
- 238000011105 stabilization Methods 0.000 description 6
- 125000000542 sulfonic acid group Chemical group 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 230000001681 protective effect Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 239000003729 cation exchange resin Substances 0.000 description 4
- 229940023913 cation exchange resins Drugs 0.000 description 4
- 238000000197 pyrolysis Methods 0.000 description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 3
- 230000003213 activating effect Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 229910052804 chromium Inorganic materials 0.000 description 3
- 239000011651 chromium Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000004132 cross linking Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 229920000620 organic polymer Polymers 0.000 description 3
- 238000009656 pre-carbonization Methods 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- 230000002028 premature Effects 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 125000003636 chemical group Chemical group 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- -1 powder Chemical compound 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000006277 sulfonation reaction Methods 0.000 description 2
- 101100008050 Caenorhabditis elegans cut-6 gene Proteins 0.000 description 1
- 235000013162 Cocos nucifera Nutrition 0.000 description 1
- 244000060011 Cocos nucifera Species 0.000 description 1
- 239000004971 Cross linker Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000000274 adsorptive effect Effects 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 238000004873 anchoring Methods 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000007857 degradation product Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000003415 peat Substances 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920005990 polystyrene resin Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000003053 toxin Substances 0.000 description 1
- 231100000765 toxin Toxicity 0.000 description 1
- 108700012359 toxins Proteins 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
- 239000002916 wood waste Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/20—Details, accessories, or equipment peculiar to rotary-drum furnaces
- F27B7/22—Rotary drums; Supports therefor
- F27B7/2206—Bearing rings
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/14—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
- F27B7/16—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means
- F27B7/161—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means the means comprising projections jutting out from the wall
- F27B7/162—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means the means comprising projections jutting out from the wall the projections consisting of separate lifting elements, e.g. lifting shovels
Definitions
- the present invention relates to a rotary tube, in particular for a rotary kiln for the production of activated carbon, according to the preamble of claim 1 and a rotary kiln with such a rotary tube. Furthermore, the present invention relates to the use of this rotary tube or rotary kiln for the production of activated carbon.
- Activated carbon is the most widely used adsorbent due to its rather nonspecific adsorptive properties. Legal requirements, but also the increasing awareness of the responsibility for the environment, lead to an increasing need for activated carbon.
- the activated carbon is increasingly being used both in the civilian as well as in the military field.
- activated carbon is used, for example, for the purification of gases, filter systems for air conditioning, car filters, etc.
- protective materials of all kinds eg respirators, protective covers and protective clothing of all kinds, such as eg protective suits etc.
- Activated carbon is generally obtained by carbonation (also referred to synonymously as carbonization, pyrolysis or coking) and subsequent activation of suitable carbonaceous starting materials. In this case, those starting materials are preferred which lead to economically reasonable yields. Because the weight loss by elimination of volatile components in the carbonization and by the burn-off when activating are significant.
- carbonation also referred to synonymously as carbonization, pyrolysis or coking
- suitable carbonaceous starting materials are preferred which lead to economically reasonable yields. Because the weight loss by elimination of volatile components in the carbonization and by the burn-off when activating are significant.
- activated carbon reference can be made, for example, to H. v. Chem. Kienle and E. Baths, activated carbon and their industrial application, Enke Verlag Stuttgart, 1980.
- Activated carbon is used in various forms: powdered coal, chipping coal, grain carbon, carbon and since the late 1970s also grain and spherical activated carbon (so-called “coal” or “carbon”).
- Grain-shaped, in particular spherical activated carbon has over a number of advantages over other forms of activated carbon such as powder, chipping coal and the like, which makes them valuable or even indispensable for certain applications: it is free-flowing, highly abrasion-resistant and dust-free and very hard.
- Grain, especially ball coal because of their special shape, but also because of the extremely high abrasion resistance for special applications, such.
- As surface filter materials for protective suits against chemical toxins or filters for low pollutant concentrations in large quantities of air very popular.
- activated carbon in particular granular carbon and spherical carbon
- suitable polymers Preference is given to using sulfonated polymers, in particular sulfonated divinylbenzene crosslinked styrene polymers, wherein the sulfonation can also be achieved in situ in the presence of sulfuric acid or oleum.
- sulfonated polymers in particular sulfonated divinylbenzene crosslinked styrene polymers, wherein the sulfonation can also be achieved in situ in the presence of sulfuric acid or oleum.
- ion exchange resins or their precursors which is usually divinylbenzene crosslinked polystyrene resins, wherein in the case of the finished ion exchanger, the sulfonic acid groups are already present in the material and in the case of IonenServormen still need to be introduced by sulfonation.
- the sulfonic acid groups play a crucial role as they play the role of a crosslinker by cleavage during carbonation. Disadvantageous and problematic, however, are in particular the large amounts of sulfur dioxide released and, among other things, the associated corrosion problems in the production equipment.
- activated carbon takes place in rotary kilns. These have, for example, a point of entry for the raw material feed at the beginning of the oven and a discharge point for the end product at the end of the oven.
- the conversion of the carbonaceous feedstock to carbon occurs, in other words, the feedstock is charred.
- Suitable starting polymers of the abovementioned type are, in particular, ion exchange resins (for example cation exchange resins or acidic ion exchange resins, preferably with sulfonic acid groups, for example cation exchange resins based on sulfonated styrene / divinylbenzene copolymers) or their precursors (ie the unsulfonated ion exchange resins which are present or in the carbonation still with a suitable sulfonating agent, such as sulfuric acid and / or oleum, must be sulfonated).
- a suitable sulfonating agent such as sulfuric acid and / or oleum
- the pyrolysis is carried out under an inert atmosphere (eg nitrogen) or at best a slightly oxidizing atmosphere.
- Carbonation is then followed by activation of the carbonated starting material.
- the basic principle of activation is to selectively and selectively degrade part of the carbon generated during carbonization under suitable conditions. This creates numerous pores, Crevices and cracks, and the unit mass surface of the activated carbon increases significantly. During activation, a targeted burning of the coal is thus carried out. Since carbon is degraded upon activation, this process results in a sometimes considerable loss of substance which, under optimum conditions, is equivalent to an increase in porosity and an increase in the internal surface area (pore volume) of the activated carbon.
- the activation therefore takes place under selective or controlled oxidizing conditions.
- Common activating gases are generally oxygen, in particular in the form of air, water vapor and / or carbon dioxide and mixtures of these activating gases.
- inert gases eg nitrogen
- the activation is generally carried out at relatively high temperatures, in particular in the temperature range from 700 ° C to 1200 ° C, preferably 800 ° C to 1100 ° C. This places high demands on the temperature resistance of the Trohrohrofenmaterials.
- the rotary kiln material must withstand the very corrosive conditions of the carbonation phase as well as the high temperature conditions of the activation phase on the one hand, only those materials are used for the production of the rotary kiln, which have a good high temperature corrosion resistance, d. H. in particular steels, which combine a good resistance to chemically aggressive materials, in particular a good corrosion resistance, as well as a good high temperature resistance in a single material.
- the present invention proposes a rotary tube according to claim 1. Further, advantageous embodiments are the subject of the relevant subclaims.
- Another object of the present invention is a rotary kiln according to claim 11, which comprises the rotary tube according to the present invention.
- Another object of the present invention is the use of the rotary tube or rotary kiln according to the invention for the production of activated carbon according to claim 12. Further, advantageous embodiments of the inventive use are the subject of the use subclaim.
- the present invention - according to a first aspect of the present invention - is thus a rotary tube, in particular for a rotary kiln for the production of activated carbon, wherein the rotary tube is provided on the outside with at least one reinforcing element for stabilizing the rotary tube in the operating state.
- a rotary tube is provided with reinforcing elements, which is dimensionally stable in the operating state, in particular under extreme temperature conditions and has a high resistance to deformation.
- the Applicant has surprisingly found that the mechanical stability or the dimensional stability of the rotary tube in the operating state, especially under extreme conditions (such as occur in activated carbon production, for example), can be considerably improved if the rotary tube on its outside or Outside wall is provided with at least one reinforcing element, preferably with a plurality of reinforcing elements.
- a rotary tube which can better resist mechanical deformation and is more resistant to strong pressure differences and pressure fluctuations and thus is dimensionally stable under operating conditions.
- the rotary tube according to the invention consequently has an improved service life with a reduced tendency for premature material fatigue. As a result, the process control and process control are facilitated.
- FIGS. 3A to 3C show a rotary tube 1 according to the present invention which can be used in a rotary kiln for the production of activated carbon.
- the rotary tube 1 according to the invention is provided on the outside with at least one reinforcing element 8 for stabilizing the rotary tube 1 in the operating state.
- mixing elements 3 for the circulation or mixing of loading material 4 located in the interior 2 of the rotary tube 1 can be arranged in the interior 2 of the rotary tube 1.
- the mixing elements 3 may be, for example, circulating or turning sheets, which are also referred to as material guide sheets, synonymously.
- the rotary tube 1 may have openings 5, which serve to receive fastening sections 6 of the mixing elements 3.
- the fastening sections 6 of the mixing elements 3 are preferably welded to the rotary tube 1 on the outside.
- the mixing elements 3 pass through the rotary tube 1 radially and in particular are welded to the rotary tube 1 on the outside or on the outside.
- the rotary tube 1 can be designed in particular as shown in the DE 10 2004 036 109.6 of 24 July 2004 is described, the entire disclosure of which is hereby incorporated by reference.
- the reinforcing element 8 serves for the mechanical stabilization of the rotary tube 1, in particular when it is exposed in the operating state to high temperatures and strong pressure fluctuations or pressure differences.
- the inventive equipment of the rotary tube 1 with at least one reinforcing element 8 is compared to the prior art significantly improved dimensional stability or resistance of the rotary tube 1 against deformation, especially in the operating state guaranteed.
- the reinforcing element 8 may be formed such that the rotary tube 1 is stabilized in its cross section and / or in its longitudinal extent. As in the Fig. 1 2A and 2B, the reinforcing member 8 may extend peripherally around the rotary tube 1. In this case, the reinforcing element 8, for example, perpendicular or inclined to the axis of rotation of the Rotary tube 1 extend, whereby a gain or stabilization of the cross section of the rotary tube 1 is realized. As far as the term "peripheral" is concerned, this refers to a circumferential arrangement of the reinforcing element 8 on the outer or outer wall of the rotary tube 1.
- the reinforcing element 8 As regards the arrangement of the reinforcing element 8, this is arranged according to a preferred embodiment according to the invention coaxial with the rotary tube 1, such as Fig. 1 and 2A demonstrate. Thus, the reinforcing member 8 and the rotary tube 1 are arranged concentrically with each other in the cross-sectional area.
- the reinforcing element 8 preferably extends at least substantially completely over the circumference of the rotary tube 1. Equally, however, it is also possible in the context of the present invention that the reinforcing element 8 extends in sections, for example in segments, over the circumference of the rotary tube 1.
- Fig. 1 and Fig. 2A show that the reinforcing element 8 is formed in accordance with a ring according to the invention particularly preferred embodiment.
- the reinforcing element 8 may be formed, for example, as an annular flange or in the manner of a hollow cylinder.
- the inner diameter of the reinforcing element 8 should at least substantially correspond to the outer diameter of the rotary tube 1.
- the present invention is not limited to a ring or hollow cylindrical design of the reinforcing element 8.
- the reinforcing element 8 is rib-like or helical.
- the reinforcing element 8 extends in a manner helical in the longitudinal direction of the rotary tube 1 around its circumference; Also in this embodiment, not shown in the figures, the reinforcing element 8 and the rotary tube 1 can be coaxial with each other or arranged.
- the reinforcing element 8 may extend axially along the rotary tube 1, whereby in particular a stabilization of the rotary tube 1 is achieved in its longitudinal extent.
- the reinforcing element 8 can extend in particular over the entire length of the rotary tube 1.
- the reinforcing element 8 can be arranged on the outer wall of the rotary tube 1 in this embodiment, not shown in the figures, for example, parallel to the rotational or longitudinal axis of the rotary tube 1.
- the reinforcing element 8 as such z. B. an at least substantially rectangular cross section, wherein the cross section of the reinforcing element 8 refers to the cut surface according to a section in the radial plane of the reinforcing element 8.
- the height or width of the cross section of the reinforcing element 8 can vary within wide limits. According to the invention, the height and width of the cross section of the reinforcing element 8 can be, for example, 0.5 cm to 10 cm, preferably 0.5 cm to 8 cm, preferably 1 cm to 6 cm, particularly preferably 1 cm to 5 cm.
- the height and the width of the cross section of the reinforcing element 8 are different. It is preferred that the height of the cross section of the reinforcing element 8 is greater than its width. According to the invention, however, it is also possible in principle that the cross section of the reinforcing element 8 is at least substantially circular or round, for example in the manner of a circularly closed steel wire.
- the reinforcing element 8 is welded to the rotary tube 1 via a welded connection 9, as in FIGS Fig. 1 . 2A, 2B and 3A to 3C can be seen.
- a permanent connection between the reinforcing element 8 on the one hand and the rotary tube 1 on the other hand guaranteed.
- the welded joint 9 extends along a line of contact of the reinforcing element 8 with the rotary tube 1 without interruption, as shown in particular in the detail enlargements a) to d) Fig. 1 as in Fig. 2A you can see.
- the welded joint 9 has at least two welding layers 9a, 9b, as shown in FIG Fig. 2B and the section enlargement according to Fig. 3A you can see. In this way, so to speak, a double welded joint 9 with welding layers 9a, 9b is formed. Different materials can be used for the different welding layers 9a, 9b. For related embodiments, reference may be made to the following explanations concerning the welding of the fastening sections 6 of the mixing elements 3 to the rotary tube 1.
- connection between the reinforcing element 8 on the one hand and the rotary tube 1 are well known to those skilled in the art: For this purpose, for example, screwing, riveting and the like can be cited. According to the invention, however, such a connection between reinforcing element 8 and rotary tube 1 is preferred, which does not pierce the shell of the rotary tube 1.
- the rotary tube 1 may have a plurality of reinforcing elements 8.
- the number of reinforcing elements 8 may be in particular two to ten, preferably two to eight, particularly preferably three to six. It is inventively preferred that the reinforcing elements 8 are evenly spaced from each other or equidistant. Insofar as required by application or due to individual circumstances, an uneven spacing of the reinforcing elements 8 can equally be provided. For example, in the case of particularly stressed sections of the rotary tube 1, a larger number of reinforcing elements 8 can be fastened per unit length of the rotary tube 1.
- the reinforcing element 8 may be made of metal, preferably steel. According to the invention, the reinforcing element 8 may consist of the same material as the rotary tube 1.
- the reinforcing element 8 or the rotary tube 1 can be particularly preferably made of high temperature resistant Steel exist. Due to the same material, the reinforcing element 8 and the rotary tube 1 at least substantially equal expansion coefficients, so that no additional material stresses due to a different expansion behavior of the reinforcing element 8 on the one hand and the rotary tube 1 on the other hand occur in the operating condition, ie at very high temperatures. In addition, this improves the compatibility of the welded joint.
- the reinforcing element 8 is designed as a cooling element or heat sink for optimized temperature control or to improve the cooling behavior of the rotary tube 1.
- the reinforcing element 8 may additionally be provided with cooling fins, which lead to a better heat dissipation behavior of the reinforcing element 8 and thus of the rotary tube 1 due to the increase in surface area.
- mixing elements 3 for example turnable plates, for the circulation or thorough mixing of load 4 can be arranged in the interior 2 of the rotary tube 1.
- the mixing elements 3 can pass through the rotary tube 1 radially and in particular be welded externally to the rotary tube 1.
- the rotary tube 1 can have apertures 5 for receiving fastening sections 6 of the mixing elements 3, wherein the fastening sections 6 can be welded to the rotary tube 1 on the outside.
- the reinforcing elements 8 may be arranged in different ways on the rotary tube 1.
- FIG. 1 The detail enlargements b) to d) of Fig. 1 show embodiments according to the invention, according to which the reinforcing element 8 is externally connected to at least one attachment portion 6 and is in contact with the attachment portion 6.
- the connection of the reinforcing element 8 with the attachment portion 6 may preferably be effected by means of a welded connection, which may be a continuation of the welded connection 9.
- the outside connection of the reinforcing element 8 with at least one attachment portion 6, in particular their welding, can be done due to the inventive arrangement of the mixing elements 3 and their attachment portions 6:
- the mounting portions 6 of the mixing elements 3 project outside of the rotary tube 1.
- the welding of the mounting portions 6 is formed with the rotary tube 1 to ensure proper operation of the rotary tube 1 gas-tight.
- the section enlargement b) of Fig. 1 an arrangement according to which the attachment portion 6 extends on both sides to a certain extent perpendicular to the reinforcing element 8 and the reinforcing element 8 is thus arranged, for example at least substantially centrally to the extending in the direction of the rotational or longitudinal axis of the rotary tube 1 attachment portion 6 and the attachment portion. 6 so to speak "crosses".
- the reinforcing element 8 may have at least one recess 10 for receiving the fastening section 6.
- the reinforcing element 8 according to the invention can be permanently connected to the fastening section 6 in the region of the recess 10, for example by means of welding.
- Fig. 1 According to detail enlargement c) of Fig. 1 is an embodiment of the invention can be seen, according to which the reinforcing element 8 in the region of the attachment portion 6 has an interruption or opening.
- the cross sections of the reinforcing element 8 are to a certain extent dull on the longitudinal side of the attachment portion 6.
- a welding of the contact surfaces of reinforcing element 8 on the one hand and fastening section 6 on the other hand can be provided.
- section enlargement d) of Fig. 1 a further inventive arrangement of the reinforcing element 8 on the rotary tube 1, after which the annular reinforcing element 8 rests with its side wall on the short side of the mounting portion 6 of a mixing element 3. It can be provided that the reinforcing element 8 is welded in the region of the contact point with the attachment portion 6. Also according to this embodiment may optionally be provided a recess of the reinforcing element 8 (not shown).
- the optionally provided attachment of the reinforcing element 8 to the attachment sections 6 of the mixing elements 3 results in an additional stabilization of the rotary tube 1, since the respective elements - reinforcing element 8 on the one hand and attachment section 6 or mixing element 3 on the other hand - intermesh, so to speak, and thus to a certain extent additionally stabilize.
- a stabilization of the mechanically heavily loaded mixing elements 3 is achieved, so that thereby an additional extension of the apparatus life is ensured.
- the reinforcing element 8 can also be connected to a plurality of mixing elements 3 or their attachment sections 6 Fig. 2A the reinforcing element 8 is connected to the mixing elements 3 located at the top and bottom in the cross-sectional area, while the laterally arranged mixing elements 3 lie behind the reinforcing element 8 in the projection plane.
- the present invention also covers such embodiments, according to which at least one particular annular reinforcing element 8 is connected to a plurality of mixing elements 3 and their attachment portions 6 so that the reinforcing element 8 is otherwise spaced from the rotary tube 1 and thus effectively fixed only to the mixing elements 3 is.
- the rotary tube 1 has a plurality, for example at least two, preferably three to six annular reinforcing elements 8, in particular of preferably high temperature resistant steel, wherein the reinforcing elements 8 peripherally about the rotary tube 1 and / or perpendicular to the axis of rotation of Rotary tube 1 extend.
- the reinforcing elements 8 of the longitudinal extent of the rotary tube 1 are arranged and preferably evenly spaced from each other.
- the reinforcing elements 8 are welded to the rotary tube 1 on the outside via a welded joint 9.
- the rotary tube 1 for mechanical stabilization in particular in pressure fluctuations by externally welded to the rotary tube 1 reinforcing elements 8, for example in the form of steel rings or steel strips reinforced.
- the reinforcing elements 8 in the form of steel rings or steel strips can, for example, "cross” the mixing elements 3 and the fastening sections 6, so to speak; At these so-called “crossing areas” the steel rings or steel bands may have recesses.
- mixing elements 3 are located in the interior 2 of the rotary tube 1 and are advantageously distributed over the interior 2 of the rotary tube 1, so that an optimal circulation or mixing of the load 4 is ensured in the operating state.
- the mixing elements 3 can be permanently connected via their attachment portions 6 with the rotary tube 1 by external welding.
- the attachment portions 6 of the mixing elements 3 are so to speak pushed through the located in the wall of the rotary tube 1 openings 5 and protrude in particular on the outside a little out or forth, so that an external welding of the mounting portions 6 of the mixing elements 3 with the rotary tube 1 (ie, with the outer wall of the rotary tube 1) or the reinforcing element 8 is made possible.
- the outside attachment of the weld 7 of the mixing elements 3 is associated with a number of advantages: Firstly, the welding site or weld prevents the weld 2 in the interior of the rotary tube 1 in the operating state prevailing aggressive conditions in the activated carbon production - corrosive acid Gases and high temperatures - is exposed. By attaching the outside welding, it is also possible to easily maintain this from the outside - even in the operating condition - to check or repair and repair if necessary. Finally, optimum welding materials can be used in this way, which ensure a good and safe permanent connection mixing elements 3 / rotary tube 1 or mixing elements 3 / reinforcing elements 8, but otherwise not permanently readily in operation 2 prevailing corrosive high temperature conditions inside the rotary tube 1 would withstand.
- a welded section 7 advantageously has at least two welding layers or two welds 7a, 7b.
- the two welding layers or welds 7a, 7b are advantageously arranged or applied one above the other. This results in double welding layers or welds 7a, 7b. This has the advantage that different materials can be used for the different welding layers 7a, 7b.
- welding materials of different temperature and corrosion resistance can be used or combined with each other, wherein the inner welding layer 7a should advantageously be corrosion and high temperature resistant, while a corrosion resistance in the outer welding layer 7b is not required to the same extent.
- a tight, in particular gas-tight and reliable welding of the connecting sections 6 of the mixing elements 3 with the rotary tube 1 is achieved.
- the inner welding layer 7a is austenitic, in particular fully austenitic, and the outer welding layer 7b is formed in a ferritic-austenitic manner.
- the welding takes place by build-up welding (eg by electrode welding).
- the welding is carried out in such a way that the shit portion 7 is formed at least substantially gas-tight.
- the fixing portions 6 of the mixing elements 3 are formed so as to protrude on the outside.
- the fastening portions 6 protrude beyond the outer wall of the rotary tube 1 or out, which allows a good weldability and a good anchoring of the mounting portions 6.
- the apertures 5 in the wall of the rotary tube 1, which serve to receive the mounting portions 6 of the mixing elements 3, are formed generally slit-like.
- the fastening portions 6 of the mixing elements 3 can be inserted, advantageously so that the mounting portions 6 project, ie protrude a little from the outer casing of the rotary tube, so that they can be better welded. This is in the FIGS. 2A and 2B seen.
- attachment portions 6 of the mixing elements 3 various embodiments are possible to ensure a secure connection of the attachment portions 6 to the rotary tube 1: some of them are in the Figs. 3A to 3C shown.
- the attachment portions 6 of the mixing elements 3 extend over the entire investment or circumferential length of the mixing elements 3; In this case, the fastening portions 6 are completely inserted through the apertures 5 in the wall of the rotary kiln 1, and such an embodiment is in Fig. 3A shown.
- the fixing portions 6 are shorter than the abutment or peripheral length of the mixing elements 3; Such embodiments are in the Figs. 3B and 3C shown. In the latter cases according to Figs.
- the mixing elements 3 can have a shoulder at the transition to the fastening cut 6, which serves in particular for contact with the inner side or inner wall of the rotary tube 1. It is also possible that the mixing elements 3 each have a plurality of engaging in different openings 5 mounting portions 6, as for example in Fig. 3C is shown.
- the mixing elements 3 may be formed, for example, like a blade or plate, in order to ensure a safe and intensive mixing and circulation of the load 4.
- the mixing elements extend at least substantially in the radial direction of the rotary tube 1, which ensures a particularly intensive mixing of the load 4.
- mixing elements 3 for example, sheets, in particular angled sheets (angle plates), can be used, which mix the loading material 4 in the manner of a blade. This is known to the skilled person as such.
- the mixing elements 3 and the reinforcing element 8 are concerned, they advantageously consist of high-temperature and corrosion-resistant material, in particular steel.
- the rotary tube 1 and the mixing elements 3 must withstand the extremely corrosive conditions of the carbonation phase and the high temperature conditions of the activation phase in the production of activated carbon.
- suitable high temperature and corrosion resistant steels from which the rotary tube 1 and / or the mixing elements 3 and / or the reinforcing element (s) 8 can be made are high alloyed steels, i. H. Steels with more than 5% alloying elements.
- Examples include high-alloy chromium and chromium / nickel steels, preferably with a chromium and / or nickel content of more than 10%, in particular more than 15%, particularly preferably more than 20%, based on the alloy. Preference is given to using ferritic or ferritic-austenitic steels with good corrosion and high-temperature behavior as the material for the production of the rotary tube 1 and / or the mixing elements 3 and / or the reinforcing element (s) 8.
- the rotary tube 1 advantageously has inlet and outlet devices for introducing and discharging as well as passing gases, for example for introducing inert gases for the carbonization phase in the activated carbon production and for introducing oxidizing gases for the activation phase in activated carbon production. This is not shown in the figures.
- this may have in the wall of the rotary tube a so-called manhole, which is sealed to the rotary tube 1 and thus allows the entry of maintenance personnel in the interior 2 of the rotary tube 1 outside of operation. This is also not shown in the figures. In this way, maintenance of the interior 2 of the rotary tube 1 is ensured in a simple manner.
- the rotary tube 1 according to the present invention is used particularly in rotary kilns for the production of activated carbon.
- the subject of the present invention - according to a second aspect of the present invention - is thus a rotary kiln having the previously described rotary tube 1 according to the present invention.
- Another object of the present invention - according to a third aspect of the invention - is the use of a rotary tube 1 as described above or of this rotary tube 1 contained rotary kiln for the production of activated carbon.
- the production of the activated carbon is generally carried out by carbonization (synonymously also referred to as pyrolysis, carbonization or coking) and subsequent activation of carbonaceous starting materials, in particular organic polymers, such.
- Sulfonated organic polymers eg, sulfonated divinylbenzene cross-linked polystyrenes which are carbonated in the rotary kiln of the present invention and subsequently activated.
- the carbonization is generally carried out at temperatures of 100 ° C to 750 ° C, in particular 150 ° C to 650 ° C, preferably 200 ° C to 600 ° C, preferably under inert or at best slightly oxidizing atmosphere, as in the introductory part described. Carbonation may be preceded by a stage of precarbonization or pre-carbonization. In contrast, the activation is generally carried out at temperatures of 700 ° C to 1200 ° C, in particular 800 ° C to 1100 ° C, preferably 850 ° C to 1000 ° C. The carbonation is - as described in the introductory part - generally under controlled or selectively oxidizing Conditions, in particular under controlled oxidizing atmosphere performed.
- Suitable starting polymers of the abovementioned type are, in particular, ion exchange resins (for example cation exchange resins or acidic ion exchange resins, preferably with sulfonic acid groups, for example cation exchange resins based on sulfonated styrene / divinylbenzene copolymers) or their precursors (ie the unsulfonated ion exchange resins which before or during the carbonation process, it may be necessary to sulfonate it with a suitable sulfonating agent, such as, for example, sulfuric acid and / or oleum.
- a suitable sulfonating agent such as, for example, sulfuric acid and / or oleum.
- a rotary tube is provided which can better resist mechanical deformation and is more resistant to strong pressure differences and pressure fluctuations and thus is dimensionally stable under operating conditions.
- the rotary tube according to the invention consequently has an improved service life with a reduced tendency for premature material fatigue. As a result, the process control and process control are facilitated.
- the rotary kiln of the present invention enables the production of activated carbon from suitable carbonaceous raw materials by carbonization and subsequent activation in a single apparatus with relatively easy handling.
Description
Die vorliegende Erfindung betrifft ein Drehrohr, insbesondere für einen Drehrohrofen zur Herstellung von Aktivkohle, nach dem Oberbegriff des Anspruchs 1 sowie einen Drehrohrofen mit einem solchen Drehrohr. Des weiteren betrifft die vorliegende Erfindung die Verwendung dieses Drehrohres bzw. Drehrohrofens zur Herstellung von Aktivkohle.The present invention relates to a rotary tube, in particular for a rotary kiln for the production of activated carbon, according to the preamble of
Aktivkohle ist aufgrund ihrer recht unspezifischen adsorptiven Eigenschaften das am meisten angewandte Adsorbens. Gesetzliche Auflagen, aber auch das steigende Bewußtsein der Verantwortung für die Umwelt, führen zu einem steigenden Bedarf an Aktivkohle.Activated carbon is the most widely used adsorbent due to its rather nonspecific adsorptive properties. Legal requirements, but also the increasing awareness of the responsibility for the environment, lead to an increasing need for activated carbon.
Dabei wird die Aktivkohle zunehmend sowohl im zivilen wie auch im militärischen Bereich angewendet. Im zivilen Bereich kommt die Aktivkohle beispielsweise für die Aufreinigung von Gasen, Filteranlagen für die Klimatisation, Autofiltern etc. zur Anwendung, während im militärischen Bereich die Aktivkohle Verwendung in Schutzmaterialien aller Art findet (z. B. Atemschutzmasken, Schutzabdeckungen und Schutzbekleidungsstücken aller Art, wie z. B. Schutzanzügen etc.)The activated carbon is increasingly being used both in the civilian as well as in the military field. In the civil sector, activated carbon is used, for example, for the purification of gases, filter systems for air conditioning, car filters, etc., while in the military area the activated carbon is used in protective materials of all kinds (eg respirators, protective covers and protective clothing of all kinds, such as eg protective suits etc.)
Aktivkohle wird im allgemeinen durch Carbonisierung (synonym auch als Schwelung, Pyrolyse oder Verkokung bezeichnet) und nachfolgende Aktivierung geeigneter kohlenstoffhaltiger Ausgangsmaterialien erhalten. Dabei werden solche Ausgangsmaterialien bevorzugt, die zu ökonomisch vernünftigen Ausbeuten führen. Denn die Gewichtsverluste durch Abspalten flüchtiger Bestandteile bei der Carbonisierung und durch den Abbrand beim Aktivieren sind erheblich. Für weitere Einzelheiten zur Herstellung von Aktivkohle kann beispielsweise verwiesen werden auf H. v. Kienle und E. Bäder, Aktivkohle und ihre industrielle Anwendung, Enke Verlag Stuttgart, 1980.Activated carbon is generally obtained by carbonation (also referred to synonymously as carbonization, pyrolysis or coking) and subsequent activation of suitable carbonaceous starting materials. In this case, those starting materials are preferred which lead to economically reasonable yields. Because the weight loss by elimination of volatile components in the carbonization and by the burn-off when activating are significant. For further details on the production of activated carbon, reference can be made, for example, to H. v. Chem. Kienle and E. Baths, activated carbon and their industrial application, Enke Verlag Stuttgart, 1980.
Die Beschaffenheit der erzeugten Aktivkohle ― fein- oder grobporig, fest oder brüchig etc. ― hängt vom kohlenstoffhaltigen Ausgangsmaterial ab. Übliche Ausgangsmaterialien sind beispielsweise Kokosnußschalen, Holzabfälle, Torf, Steinkohle, Peche, aber auch besondere Kunststoffe, wie z. B. sulfonierte Polymere, die unter anderem bei der Herstellung von Aktivkohle in Form von Körnchen oder Kügelchen eine große Rolle spielen.The nature of the activated carbon produced - fine or coarsely porous, solid or brittle, etc. - depends on the carbonaceous starting material. Typical starting materials are, for example, coconut shells, wood waste, peat, hard coal, pitches, but also special plastics such. As sulfonated polymers that play a major role in the production of activated carbon in the form of granules or beads, inter alia.
Aktivkohle wird in verschiedenen Formen verwendet: Pulverkohle, Splitterkohle, Kornkohle, Formkohle und seit Ende der 1970er Jahre auch korn- und kugelförmige Aktivkohle (sogenannte "Kornkohle" bzw. "Kugelkohle"). Kornförmige, insbesondere kugelförmige Aktivkohle hat gegenüber anderen Formen von Aktivkohle wie Pulver-, Splitterkohle und dergleichen eine Reihe von Vorteilen, die sie für bestimmte Applikationen wertvoll oder sogar unverzichtbar macht: Sie ist rieselfähig, enorm abriebfest und staubfrei und sehr hart. Kornkohle, insbesondere Kugelkohle, ist wegen ihrer speziellen Form, aber auch wegen der extrem hohen Abriebfestigkeit für besondere Einsatzgebiete, so z. B. Flächenfiltermaterialien für Schutzanzüge gegen chemische Gifte oder Filter für niedrige Schadstoffkonzentrationen in großen Luftmengen, sehr gefragt.Activated carbon is used in various forms: powdered coal, chipping coal, grain carbon, carbon and since the late 1970s also grain and spherical activated carbon (so-called "coal" or "carbon"). Grain-shaped, in particular spherical activated carbon has over a number of advantages over other forms of activated carbon such as powder, chipping coal and the like, which makes them valuable or even indispensable for certain applications: it is free-flowing, highly abrasion-resistant and dust-free and very hard. Grain, especially ball coal, because of their special shape, but also because of the extremely high abrasion resistance for special applications, such. As surface filter materials for protective suits against chemical toxins or filters for low pollutant concentrations in large quantities of air, very popular.
Bei der Herstellung von Aktivkohle, insbesondere Kornkohle und Kugelkohle, wird in den meisten Fällen von geeigneten Polymeren ausgegangen. Bevorzugt kommen sulfonierte Polymere, insbesondere sulfonierte divinylbenzolvernetze Styrolpolymere, zum Einsatz, wobei die Sulfonierung auch in situ in Gegenwart von Schwefelsäure bzw. Oleum erreicht werden kann. Als geeignetes Ausgangsmaterial dienen z. B. Ionenaustauscherharze bzw. deren Vorstufen, bei denen es sich zumeist um divinylbenzolvernetzte Polystyrolharze handelt, wobei im Falle der fertigen Ionenaustauscher die Sulfonsäuregruppen bereits im Material vorhanden sind und im Falle der Ionenaustauschervorstufen noch durch Sulfonierung eingeführt werden müssen. Die Sulfonsäuregruppen spielen eine entscheidende Funktion, da ihnen die Rolle eines Vernetzers zukommen, indem sie bei der Carbonisierung abgespalten werden. Nachteilig und problematisch sind aber insbesondere die großen Mengen an freigesetzten Schwefeldioxid sowie die damit unter anderem verbundenen Korrosionsprobleme in den Herstellapparaturen.In the production of activated carbon, in particular granular carbon and spherical carbon, it is assumed in most cases of suitable polymers. Preference is given to using sulfonated polymers, in particular sulfonated divinylbenzene crosslinked styrene polymers, wherein the sulfonation can also be achieved in situ in the presence of sulfuric acid or oleum. As a suitable starting material serve z. B. ion exchange resins or their precursors, which is usually divinylbenzene crosslinked polystyrene resins, wherein in the case of the finished ion exchanger, the sulfonic acid groups are already present in the material and in the case of Ionenaustauschervorstufen still need to be introduced by sulfonation. The sulfonic acid groups play a crucial role as they play the role of a crosslinker by cleavage during carbonation. Disadvantageous and problematic, however, are in particular the large amounts of sulfur dioxide released and, among other things, the associated corrosion problems in the production equipment.
Üblicherweise erfolgt die Herstellung von Aktivkohle in Drehrohröfen. Diese weisen beispielsweise eine Eintragsstelle für die Rohstoffbeschickung am Ofenanfang und eine Austragsstelle für das Endprodukt am Ofenende auf.Usually, the production of activated carbon takes place in rotary kilns. These have, for example, a point of entry for the raw material feed at the beginning of the oven and a discharge point for the end product at the end of the oven.
Bei den herkömmlichen Prozessen zur Herstellung von Aktivkohle nach dem Stand der Technik werden bei der diskontinuierlichen Herstellung sowohl die Carbonisierung als auch die nachfolgende Aktivierung in einem Drehrohr durchgeführt.In the conventional processes for producing activated carbon according to the prior art, in the batchwise production, both the carbonization and the subsequent activation are carried out in a rotary kiln.
Bei der Carbonisierung, welcher einer Phase der Vorcarbonisierung bzw. Vorschwelung vorangehen kann, erfolgt die Umwandlung des kohlenstoffhaltigen Ausgangsmaterials zu Kohlenstoff, d. h. mit anderen Worten wird das Ausgangsmaterial verkohlt. Bei der Carbonisierung der zuvor genannten organischen Polymere auf Basis von Styrol und Divinylbenzol, die vernetzende funktionelle chemische Gruppen, welche bei ihrer thermischen Zersetzung zu freien Radikalen und somit zu Vernetzungen führen, insbesondere Sulfonsäuregruppen, enthalten, werden ― unter Abspaltung flüchtiger Bestandteile, wie insbesondere SO2 ― die funktionellen chemischen Gruppen, insbesondere Sulfonsäuregruppen, zerstört, und es bilden sich freie Radikale, die eine starke Vernetzung bewirken ― ohne die es keinen Pyrolyserückstand (= Kohlenstoff) gäbe. Geeignete Ausgangspolymere der vorgenannten Art sind insbesondere Ionenaustauscherharze (z. B. Kationenaustauscherharze bzw. saure Ionenaustauscherharze, vorzugsweise mit Sulfonsäuregruppen, so z. B. Kationenaustauscherharze auf Basis sulfonierter Styrol/Divinylbenzol-Copolymere) bzw. deren Vorstufen (d. h. die unsulfonierten Ionenaustauscherharze, welche vor oder bei der Carbonisierung noch mit einem geeigneten Sulfonierungsmittel, wie z. B. Schwefelsäure und/oder Oleum, sulfoniert werden müssen). Im allgemeinen wird die Pyrolyse unter inerter Atmosphäre (z. B. Stickstoff) oder allenfalls leicht oxidierender Atmosphäre durchgeführt. Gleichermaßen kann es vorteilhaft sein, während der Carbonisierung, insbesondere bei höheren Temperaturen (z. B. im Bereich von etwa 500 °C bis 650 °C), zu der Inertatmosphäre eine kleinere Menge an Sauerstoff, insbesondere in Form von Luft (z. B. 1 bis 5 %), zuzugeben, um eine Oxidation des carbonisierten Polymerskeletts zu bewirken und auf diese Weise die nachfolgende Aktivierung zu erleichtem.In carbonization, which may precede a pre-carbonization phase, the conversion of the carbonaceous feedstock to carbon occurs, in other words, the feedstock is charred. In the carbonization of the aforementioned organic polymers based on styrene and divinylbenzene, the crosslinking functional chemical groups which in their thermal decomposition to free radicals and thus lead to crosslinking, in particular sulfonic acid groups, are - with elimination of volatile components, in particular SO 2 - destroys the functional chemical groups, in particular sulfonic acid groups, and free radicals form, which cause strong crosslinking - without which there would be no pyrolysis residue (= carbon). Suitable starting polymers of the abovementioned type are, in particular, ion exchange resins (for example cation exchange resins or acidic ion exchange resins, preferably with sulfonic acid groups, for example cation exchange resins based on sulfonated styrene / divinylbenzene copolymers) or their precursors (ie the unsulfonated ion exchange resins which are present or in the carbonation still with a suitable sulfonating agent, such as sulfuric acid and / or oleum, must be sulfonated). In general, the pyrolysis is carried out under an inert atmosphere (eg nitrogen) or at best a slightly oxidizing atmosphere. Similarly, during carbonation, especially at higher temperatures (eg, in the range of about 500 ° C to 650 ° C), it may be advantageous to add a smaller amount of oxygen to the inert atmosphere, particularly in the form of air (e.g. 1 to 5%) to effect oxidation of the carbonized polymer skeleton and thus facilitate subsequent activation.
Aufgrund der bei der Carbonisierung abgespaltenen sauren Reaktionsprodukte (z. B. SO2) ist diese Stufe des Herstellungsprozesses der Aktivkohle extrem korrosiv in bezug auf das Ofenmaterial und stellt höchste Ansprüche in bezug auf die Korrosionsbeständigkeit des Drehrohrofenmaterials.Due to the acidic reaction products (eg SO 2 ) removed during the carbonation, this stage of the activated carbon production process is extremely corrosive with respect to the furnace material and places the highest demands on the corrosion resistance of the rotary kiln material.
Der Carbonisierung schließt sich dann die Aktivierung des carbonisierten Ausgangsmaterials an. Das Grundprinzip der Aktivierung besteht darin, einen Teil des bei der Schwelung generierten Kohlenstoffs selektiv und gezielt unter geeigneten Bedingungen abzubauen. Hierdurch entstehen zahlreiche Poren, Spalten und Risse, und die auf die Masseneinheit bezogene Oberfläche der Aktivkohle nimmt erheblich zu. Bei der Aktivierung wird also ein gezielter Abbrand der Kohle vorgenommen. Da bei der Aktivierung Kohlenstoff abgebaut wird, tritt bei diesem Vorgang ein zum Teil erheblicher Substanzverlust ein, welcher unter optimalen Bedingungen gleichbedeutend mit einer Erhöhung der Porosität ist und eine Zunahme der inneren Oberfläche (Porenvolumen) der Aktivkohle bedeutet. Die Aktivierung erfolgt daher unter selektiv bzw. kontrolliert oxidierenden Bedingungen. Übliche Aktivierungsgase sind im allgemeinen Sauerstoff, insbesondere in Form von Luft, Wasserdampf und/oder Kohlendioxid sowie Gemischen diese Aktivierungsgase. Den Aktivierungsgasen können gegebenenfalls Inertgase (z. B. Stickstoff) zusesetzt werden. Um eine technisch ausreichend hohe Reaktionsgeschwindigkeit zu erzielen, wird die Aktivierung im allgemeinen bei relativ hohen Temperaturen durchgeführt, insbesondere im Temperaturbereich von 700 °C bis 1.200 °C, vorzugsweise 800 °C bis 1.100 °C. Dies stellt hohe Anforderungen an die Temperaturbeständigkeit des Drohrohrofenmaterials.Carbonation is then followed by activation of the carbonated starting material. The basic principle of activation is to selectively and selectively degrade part of the carbon generated during carbonization under suitable conditions. This creates numerous pores, Crevices and cracks, and the unit mass surface of the activated carbon increases significantly. During activation, a targeted burning of the coal is thus carried out. Since carbon is degraded upon activation, this process results in a sometimes considerable loss of substance which, under optimum conditions, is equivalent to an increase in porosity and an increase in the internal surface area (pore volume) of the activated carbon. The activation therefore takes place under selective or controlled oxidizing conditions. Common activating gases are generally oxygen, in particular in the form of air, water vapor and / or carbon dioxide and mixtures of these activating gases. If desired, inert gases (eg nitrogen) may be used in the activation gases. In order to achieve a technically sufficiently high reaction rate, the activation is generally carried out at relatively high temperatures, in particular in the temperature range from 700 ° C to 1200 ° C, preferably 800 ° C to 1100 ° C. This places high demands on the temperature resistance of the Trohrohrofenmaterials.
Da das Drehrohrofenmaterial also einerseits den sehr korrosiven Bedingungen der Carbonisierungsphase als auch den Hochtemperaturbedingungen der Aktivierungsphase standhalten muß, kommen für die Herstellung des Drehrohrofens nur solche Materialien zum Einsatz, welche eine gute Hochtemperaturkorrosionsbeständigkeit aufweisen, d. h. insbesondere Stähle, welche eine gute Beständigkeit gegenüber chemisch aggressiven Materialien, insbesondere eine gute Korrosionsbeständigkeit, sowie eine gute Hochtemperaturbeständigkeit in einem einzigen Material vereinen.Since the rotary kiln material must withstand the very corrosive conditions of the carbonation phase as well as the high temperature conditions of the activation phase on the one hand, only those materials are used for the production of the rotary kiln, which have a good high temperature corrosion resistance, d. H. in particular steels, which combine a good resistance to chemically aggressive materials, in particular a good corrosion resistance, as well as a good high temperature resistance in a single material.
Trotz der Hochtemperaturbeständigkeit der für das Drehrohr üblicherweise eingesetzten Materialien, insbesondere Stahl, führen die hohen Betriebstemperaturen bei der Aktivkohleherstellung, die bis zu 1.200 °C oder sogar mehr erreichen können, dazu, daß diese Materialien bzw. der Stahl unter diesen extremen Temperaturen relativ weich werden und an Formstabilität verlieren und infolgedessen zu einer gewissen Anfälligkeit in bezug auf mechanische Deformationen neigen. Verfahrensimmanent treten bei der Aktivherstellung starke Druckdifferenzen und Druckschwankungen auf: Dies ist insbesondere dadurch bedingt, daß einerseits gasförmige Abbauprodukte generiert werden und andererseits Reaktions- bzw. Prozeßgase zugeführt werden müssen und unter wechselnden Druckbedingungen (z. B. Atmosphärendruck und reduziertem Druck bzw. Vakuum) gearbeitet wird, wobei die Druckverhältnisse nicht über die gesamte Verfahrensdauer der Aktivkohleherstellung konstantgehalten werden können. Dies führt teilweise dazu, daß die nicht unerheblichen Druckdifferenzen und Druckschwankungen im Betriebszustand eine Deformation des Drehrohres bewirken können. Dies kann zu Schäden an der Drehrohrapparatur und zu einer vorzeitigen Materialermüdung führen, und zum anderen sind die Prozeßführung und die Prozeßkontrolle hierdurch nicht unerheblich erschwert.Despite the high temperature resistance of the materials commonly used for the rotary kiln, especially steel, the high operating temperatures in activated carbon production, which can reach up to 1200 ° C or even more, make these materials or steel relatively soft under these extreme temperatures and lose shape stability and, as a result, tend to have some susceptibility to mechanical deformation. Process inherent occur in the active production of strong pressure differences and pressure fluctuations: This is due in particular to the fact that on the one hand gaseous degradation products are generated and on the other hand reaction or process gases must be supplied and operating under changing pressure conditions (eg atmospheric pressure and reduced pressure or vacuum), wherein the pressure conditions can not be kept constant over the entire process time of the activated carbon production. This leads in part to the fact that the not insignificant pressure differences and pressure fluctuations in the operating state can cause a deformation of the rotary tube. This can lead to damage to the rotary kiln and premature material fatigue, and on the other hand, the process control and process control are not significantly hampered.
Eine Aufgabe der vorliegenden Erfindung liegt somit darin, eine Apparatur bzw. ein Drehrohr zur Verfügung zu stellen, welche bzw. welches sich insbesondere für die Herstellung von Aktivkohle eignet, wobei die zuvor geschilderten Nachteile des Standes der Technik zumindest teilweise vermieden oder aber wenigstens abgeschwächt werden sollen.It is therefore an object of the present invention to provide an apparatus or a rotary tube which is particularly suitable for the production of activated carbon, wherein the previously described disadvantages of the prior art are at least partially avoided or at least mitigated should.
Zur Lösung des zuvor geschilderten Problems schlägt die vorliegende Erfindung ein Drehrohr nach Anspruch 1 vor. Weitere, vorteilhafte Ausgestaltungen sind Gegenstand der diesbezüglichen Unteransprüche.To solve the above problem, the present invention proposes a rotary tube according to
Weiterer Gegenstand der vorliegenden Erfindung ist ein Drehrohrofen nach Anspruch 11, welcher das Drehrohr nach der vorliegenden Erfindung umfaßt.Another object of the present invention is a rotary kiln according to claim 11, which comprises the rotary tube according to the present invention.
Schließlich ist ein weiterer Gegenstand der vorliegenden Erfindung die Verwendung des erfindungsgemäßen Drehrohres bzw. Drehrohrofens zur Herstellung von Aktivkohle nach Anspruch 12. Weitere, vorteilhafte Ausgestaltungen der erfindungsgemäßen Verwendung sind Gegenstand des Verwendungsunteranspruchs.Finally, another object of the present invention is the use of the rotary tube or rotary kiln according to the invention for the production of activated carbon according to claim 12. Further, advantageous embodiments of the inventive use are the subject of the use subclaim.
Gegenstand der vorliegenden Erfindung ― gemäß einem ersten Aspekt der vorliegenden Erfindung ― ist somit ein Drehrohr, insbesondere für einen Drehrohrofen zur Herstellung von Aktivkohle, wobei das Drehrohr außenseitig mit mindestens einem Verstärkungselement zur Stabilisierung des Drehrohres im Betriebszustand versehen ist. Somit wird ein Drehrohr mit Verstärkungselementen bereitgestellt, das im Betriebszustand, insbesondere unter extremen Temperaturbedingungen, formstabil ist und eine hohe Widerstandsfähigkeit gegenüber Deformationen aufweist.The present invention - according to a first aspect of the present invention - is thus a rotary tube, in particular for a rotary kiln for the production of activated carbon, wherein the rotary tube is provided on the outside with at least one reinforcing element for stabilizing the rotary tube in the operating state. Thus, a rotary tube is provided with reinforcing elements, which is dimensionally stable in the operating state, in particular under extreme temperature conditions and has a high resistance to deformation.
Denn die Anmelderin hat überraschenderweise herausgefunden, daß die mechanische Stabilität bzw. die Formstabilität des Drehrohres im Betriebszustand, insbesondere auch unter extremen Bedingungen (wie sie z. B. bei der Aktivkohleherstellung auftreten), beträchtlich verbessert werden kann, wenn das Drehrohr an seiner Außenseite bzw. Außenwandung mit mindestens einem Verstärkungselement, vorzugsweise mit einer Mehrzahl von Verstärkungselementen, versehen wird.The Applicant has surprisingly found that the mechanical stability or the dimensional stability of the rotary tube in the operating state, especially under extreme conditions (such as occur in activated carbon production, for example), can be considerably improved if the rotary tube on its outside or Outside wall is provided with at least one reinforcing element, preferably with a plurality of reinforcing elements.
Auf diese Weise wird ein Drehrohr geschaffen, welches mechanischen Deformationen besser widerstehen kann und resistenter auch gegenüber starken Druckdifferenzen und Druckschwankungen ist und somit auch unter Betriebsbedingungen formstabil ist. Das erfindungsgemäße Drehrohr weist folglich eine verbesserte Lebensdauer mit verringerter Tendenz zur vorzeitigen Materialermüdung auf. Auch sind infolgedessen die Prozeßführung und Prozeßkontrolle erleichtert.In this way, a rotary tube is provided which can better resist mechanical deformation and is more resistant to strong pressure differences and pressure fluctuations and thus is dimensionally stable under operating conditions. The rotary tube according to the invention consequently has an improved service life with a reduced tendency for premature material fatigue. As a result, the process control and process control are facilitated.
Weitere Vorteile, Eigenschaften, Aspekte, Besonderheiten und Merkmale der vorliegenden Erfindung ergeben sich aus der folgenden Beschreibung eines in der Zeichnung dargestellten, bevorzugten Ausführungsbeispiels. Es zeigt:
- Fig. 1
- eine schematische Seitenansicht eines Drehrohrofens nach einem bevorzugten Ausführungsbeispiel der vorliegenden Erfindung im Schnitt (
Fig. 1 ) sowie Ausschnitte a), b), c) und d) von verschieden ausgebildeten, erfindungsgemäß bevorzugten Ausgestaltungen der Verstärkungselemente; - Fig. 2A
- einen radialen Querschnitt durch das Drehrohr;
- Fig. 2B
- einen vergrößerten Ausschnitt des in
Fig. 2A gekennzeichneten Bereiches; - Fig. 3A - C
- eine schematische Darstellung von Profilen von Mischelementen mit unterschiedlich ausgebildeten Befestigungsabschnitten sowie eine schematische Darstellung der Verstärkungselemente.
- Fig. 1
- a schematic side view of a rotary kiln according to a preferred embodiment of the present invention in section (
Fig. 1 ) as well as sections a), b), c) and d) of differently shaped, according to the invention preferred embodiments of the reinforcing elements; - Fig. 2A
- a radial cross section through the rotary tube;
- Fig. 2B
- an enlarged section of the in
Fig. 2A marked area; - FIGS. 3A-C
- a schematic representation of profiles of mixing elements with differently shaped mounting portions and a schematic representation of the reinforcing elements.
Wie den
Das Drehrohr 1 als solches kann insbesondere in der Art ausgebildet sein, wie es in der
Auch
Was das Verstärkungselement 8 anbelangt, so dient dieses zur mechanischen Stabilisierung des Drehrohres 1, insbesondere wenn dieses im Betriebszustand hohen Temperaturen und starken Druckschwankungen bzw. Druckdifferenzen ausgesetzt ist. Auf diese Weise wird somit aufgrund der erfindungsgemäßen Ausstattung des Drehrohres 1 mit mindestens einem Verstärkungselement 8 eine gegenüber dem Stand der Technik signifikant verbesserte Formstabilität bzw. Beständigkeit des Drehrohres 1 gegenüber Deformationen, insbesondere im Betriebszustand, gewährleistet.As far as the reinforcing
Das Verstärkungselement 8 kann derart ausgebildet sein, daß das Drehrohr 1 in seinem Querschnitt und/oder in seiner Längserstreckung stabilisiert wird. Wie in den
Was die Anordnung des Verstärkungselementes 8 betrifft, so ist dieses gemäß einer erfindungsgemäß bevorzugten Ausführungsform koaxial zum Drehrohr 1 angeordnet, wie
Weiterhin verdeutlichen die Ausschnittsvergrößerungen a) bis d) von
Die vorliegende Erfindung ist nicht auf eine ring- oder hohlzylindrische Ausbildung des Verstärkungselementes 8 beschränkt. So kann es beispielsweise auch vorgesehen sein, daß das Verstärkungselement 8 rippenartig oder schraubenlinienförmig ausgebildet ist. Bei einer schraubenlinienförmigen Ausbildung des Verstärkungselementes 8 erstreckt sich das Verstärkungselement 8 gewissermaßen helixartig in Längsrichtung des Drehrohres 1 um dessen Umfang; auch bei dieser, in den Figuren nicht dargestellten Ausführungsform können das Verstärkungselement 8 und das Drehrohr 1 koaxial zueinander verlaufen bzw. angeordnet sein.The present invention is not limited to a ring or hollow cylindrical design of the reinforcing
Gemäß einer weiteren erfindungsgemäßen Ausführungsform kann sich das Verstärkungselement 8 axial entlang des Drehrohres 1 erstrecken, wodurch insbesondere eine Stabilisierung des Drehrohres 1 in seiner Längserstreckung erreicht wird. Dabei kann sich das Verstärkungselement 8 insbesondere über die gesamte Länge des Drehrohres 1 erstrecken. Was die axiale Anordnung des Verstärkungselementes 8 betrifft, so kann das Verstärkungselement 8 bei dieser, in den Figuren nicht dargestellten Ausführungsform beispielsweise parallel zur Dreh- bzw. Längsachse des Drehrohres 1 auf der Außenwandung des Drehrohres 1 angeordnet sein.According to a further embodiment of the invention, the reinforcing
Wie
Erfindungsgemäß bevorzugt ist das Verstärkungselement 8 mit dem Drehrohr 1 über eine Schweißverbindung 9 verschweißt, wie in den
Alternativ ist aber auch eine abschnittsweise bzw. segmentartige Schweißverbindung 9 des Verstärkungselementes 8 mit dem Drehrohr 1 oder eine punktförmige Ausbildung der Schweißverbindung 9 zur dauerhaften Befestigung des Verstärkungselementes 8 auf dem Drehrohr 1 möglich.Alternatively, however, a section-wise or segment-like welded joint 9 of the reinforcing
Erfindungsgemäß kann es vorgesehen sein, daß die Schweißverbindung 9 mindestens zwei Schweißschichten 9a, 9b aufweist, wie es in
Weitere Verbindungsarten zwischen Verstärkungselement 8 einerseits und Drehrohr 1 sind dem Fachmann hinlänglich bekannt: Hierzu können beispielsweise Verschrauben, Vernieten und dergleichen angeführt werden. Erfindungsgemäß ist jedoch eine solche Verbindung zwischen Verstärkungselement 8 und Drehrohr 1 bevorzugt, welche die Hülle des Drehrohres 1 nicht durchstößt.Further types of connection between the reinforcing
Wie in der
Das Verstärkungselement 8 kann aus Metall, vorzugsweise Stahl, bestehen. Erfindungsgemäß bevorzugt kann das Verstärkungselement 8 aus demselben Material wie das Drehrohr 1 bestehen. Das Verstärkungselement 8 bzw. das Drehrohr 1 können besonders bevorzugt aus hochtemperaturbeständigem Stahl bestehen. Aufgrund des gleichen Materials weisen das Verstärkungselement 8 sowie das Drehrohr 1 zumindest im wesentlichen gleiche Ausdehnungskoeffizienten auf, so daß im Betriebszustand, d.h. bei sehr hohen Temperaturen, keine zusätzlichen Materialbeanspruchungen aufgrund eines unterschiedlichen Ausdehnungsverhalten des Verstärkungselementes 8 einerseits und des Drehrohres 1 andererseits auftreten. Außerdem wird hierdurch die Kompatibilität der Schweißverbindung verbessert.The reinforcing
Weiterhin kann es erfindungsgemäß vorgesehen sein, daß zur optimierten Temperaturkontrolle bzw. zur Verbesserung des Abkühlverhaltens des Drehrohres 1 das Verstärkungselement 8 als Kühlelement bzw. Kühlkörper ausgebildet ist. Gemäß dieser Ausführungsform kann das Verstärkungselement 8 zusätzlich mit Kühlrippen versehen sein, die aufgrund der Oberflächenvergrößerung zu einem besseren Wärmeabgabeverhalten des Verstärkungselementes 8 und damit des Drehrohres 1 führen.Furthermore, it can be inventively provided that the reinforcing
Wie zuvor ausgeführt und wie in den
Wie die Ausschnittsvergrößerungen a) bis d) von
So ist der Ausschnittsvergrößerungen a) von
Die Ausschnittsvergrößerungen b) bis d) von
Die außenseitige Verbindung des Verstärkungselementes 8 mit mindestens einem Befestigungsabschnitt 6, insbesondere deren Verschweißung, kann aufgrund der erfindungsgemäßen Anordnung der Mischelemente 3 bzw. deren Befestigungsabschnitte 6 erfolgen: Die Befestigungsabschnitte 6 der Mischelemente 3 ragen außenseitig aus dem Drehrohr 1 vor. Im Rahmen der vorliegenden Erfindung ist zu beachten, daß die Verschweißung der Befestigungsabschnitte 6 mit dem Drehrohr 1 zur Gewährleistung einer einwandfreien Funktion des Drehrohres 1 gasdicht ausgebildet ist.The outside connection of the reinforcing
Die Ausschnittsvergrößerungen b) bis d) von
So zeigt die Ausschnittsvergrößerung b) von
Gemäß Ausschnittsvergrößerung c) von
Schließlich zeigt Ausschnittsvergrößerung d) von
Durch die gegebenenfalls vorgesehene Befestigung des Verstärkungselementes 8 an den Befestigungsabschnitten 6 der Mischelemente 3 resultiert eine zusätzliche Stabilisierung des Drehrohres 1, da die jeweiligen Elemente ― Verstärkungselement 8 einerseits und Befestigungsabschnitt 6 bzw. Mischelement 3 andererseits ― sozusagen ineinandergreifen und sich somit gewissermaßen zusätzlich stabilisieren. Hierdurch wird insbesondere auch eine Stabilisierung der mechanisch stark beanspruchten Mischelemente 3 erreicht, so daß hierdurch eine zusätzliche Verlängerung der Apparaturlebensdauer gewährleistet wird.The optionally provided attachment of the reinforcing
Wie in
Die vorliegende Erfindung erfaßt auch solche Ausführungsformen, wonach mindestens ein insbesondere ringförmiges Verstärkungselement 8 mit einer Mehrzahl an Mischelementen 3 bzw. deren Befestigungsabschnitten 6 verbunden sind, so daß das Verstärkungselement 8 im übrigen von dem Drehrohr 1 beabstandet und somit gewissermaßen nur an den Mischelementen 3 fixiert ist.The present invention also covers such embodiments, according to which at least one particular annular reinforcing
Gemäß einer erfindungsgemäß besonders bevorzugten Ausführungsform weist das Drehrohr 1 eine Mehrzahl, beispielsweise mindestens zwei, vorzugsweise drei bis sechs ringförmige Verstärkungselemente 8, insbesondere aus vorzugsweise hochtemperaturbeständigen Stahl, auf, wobei sich die Verstärkungselemente 8 peripher um das Drehrohr 1 und/oder senkrecht zur Drehachse des Drehrohres 1 erstrecken. Dabei sind die Verstärkungselemente 8 der Längserstreckung des Drehrohres 1 angeordnet und vorzugsweise gleichmäßig voneinander beabstandet. Gemäß dieser besonders bevorzugten Ausfiihrungsform sind die Verstärkungselemente 8 mit dem Drehrohr 1 außenseitig über eine Schweißverbindung 9 verschweißt. Somit ist das Drehrohr 1 zur mechanischen Stabilisierung insbesondere bei Druckschwankungen durch von außen auf das Drehrohr 1 aufgeschweißte Verstärkungselemente 8, beispielsweise in der Art von Stahlringen oder Stahlbändern, verstärkt. Die Verstärkungselemente 8 in Form von Stahlringen oder Stahlbändern können beispielsweise die Mischelemente 3 bzw. die Befestigungsabschnitte 6 sozusagen "kreuzen"; an diesen sogenannten "Kreuzungsbereichen" können die Stahlringe oder Stahlbänder Aussparungen aufweisen.According to a particularly preferred embodiment according to the invention, the
Was die gemäß einer bevorzugten Ausführungsform vorgesehenen Mischelemente 3 betrifft, so sind diese im Innenraum 2 des Drehrohres 1 befindlich und sind vorteilhafterweise über den Innenraum 2 des Drehrohres 1 verteilt angeordnet, so daß eine optimale Umwälzung bzw. Durchmischung des Beladungsgutes 4 im Betriebszustand gewährleistet ist. Die Mischelemente 3 können über ihre Befestigungsabschnitte 6 mit dem Drehrohr 1 durch außenseitige Verschweißung dauerhaft verbunden sein. Die Befestigungsabschnitte 6 der Mischelemente 3 sind sozusagen durch die in der Wandung des Drehrohres 1 befindlichen Durchbrechungen 5 durchgesteckt und ragen insbesondere außenseitig ein wenig heraus bzw. hervor, so daß eine außenseitige Verschweißung der Befestigungsabschnitte 6 der Mischelemente 3 mit dem Drehrohr 1 (d. h. also mit der Außenwandung des Drehrohres 1) bzw. dem Verstärkungselement 8 ermöglicht wird.As regards the
Die außenseitige Anbringung der Verschweißung 7 der Mischelemente 3 ist mit einer Reihe von Vorteilen verbunden: Zum einen wird durch die außenseitige Verschweißung vermieden, daß die Verschweißungsstelle bzw. Schweißnaht den im Inneren 2 des Drehrohres 1 im Betriebszustand vorherrschenden aggressiven Bedingungen bei der Aktivkohleherstellung - korrosive saure Gase und hohe Temperaturen - ausgesetzt ist. Durch die außenseitige Anbringung der Verschweißung ist es außerdem möglich, diese ohne weiteres von außen ― auch im Betriebszustand ― zu warten bzw. zu überprüfen und bei Bedarf auszubessern bzw. reparieren. Schließlich können auf diese Weise optimale Schweißmaterialien zum Einsatz kommen, welche eine gute und sichere dauerhafte Verbindung Mischelemente 3/Drehrohr 1 bzw. Mischelemente 3/Verstärkungselemente 8 gewährleisten, aber ansonsten den im Betrieb vorherrschenden korrosiven Hochtemperaturbedingungen im Inneren 2 des Drehrohres 1 nicht ohne weiteres dauerhaft standhalten würden.The outside attachment of the
Wie aus
Im allgemeinen sind die Befestigungsabschnitte 6 der Mischelemente 3 derart ausgebildet, daß sie außenseitig vorragen. Mit anderen Worten ragen die Befestigungsabschnitte 6 über die äußere Wandung des Drehrohres 1 heraus bzw. hinaus, was eine gute Verschweißbarkeit und eine gute Verankerung der Befestigungsabschnitte 6 ermöglicht.In general, the fixing
Die Durchbrechungen 5 in der Wandung des Drehrohres 1, welche zur Aufnahme der Befestigungsabschnitte 6 der Mischelemente 3 dienen, sind im allgemeinen schlitzartig ausgebildet. Durch diese insbesondere schlitzartigen Durchbrechungen 5 können dann die Befestigungsabschnitte 6 der Mischelemente 3 durchgesteckt sein, vorteilhafterweise so, daß die Befestigungsabschnitte 6 vorragen, d. h. ein wenig von der äußeren Ummantelung des Drehrohres abstehen, damit sie besser verschweißt werden können. Dies ist in den
Was die Befestigungsabschnitte 6 der Mischelemente 3 anbelangt, so sind verschiedene Ausgestaltungen möglich, um eine sichere Verbindung der Befestigungsabschnitte 6 mit dem Drehrohr 1 zu gewährleisten: Einige davon sind in den
Was die Mischelemente 3 anbelangt, so können diese beispielsweise schaufel- oder plattenartig ausgebildet sein, um eine sichere und intensive durch Mischung und Umwälzung des Beladungsgutes 4 zu gewährleisten. Gemäß einer Ausführungsform verlaufen die Mischelemente zumindest im wesentlichen in Radialrichtung des Drehrohres 1, was eine besonders intensive Durchmischung des Beladungsgutes 4 gewährleistet. Als Mischelemente 3 können beispielsweise Bleche, insbesondere gewinkelte Bleche (Winkelbleche), verwendet werden, welche in der Art einer Schaufel das Beladungsgut 4 durchmischen. Dies ist dem Fachmann als solches bekannt.As far as the
Was das Drehrohr 1, die Mischelemente 3 und das Verstärkungselement 8 anbelangt, so bestehen diese vorteilhafterweise aus hochtemperatur- und korrosionsbeständigem Material, insbesondere Stahl. Denn sowohl das Drehrohr 1 als auch die Mischelemente 3 müssen den extrem korrosiven Bedingungen der Carbonisierungsphase und den Hochtemperaturbedingungen der Aktivierungsphase bei der Herstellung von Aktivkohle standhalten. Beispiele für geeignete hochtemperatur- und korrosionsbeständige Stähle, aus denen das Drehrohr 1 und/oder die Mischelemente 3 und/oder das bzw. die Verstärkungselemente 8 hergestellt werden können, sind hochlegierte Stähle, d. h. Stähle mit mehr als 5 % Legierungselementen. Beispiele hierfür sind hochlegierte Chrom- und Chrom/Nickel-Stähle, vorzugsweise mit einem Chrom- und/oder Nickelanteil über 10 %, insbesondere über 15 %, besonders bevorzugt über 20 %, bezogen auf die Legierung. Bevorzugt werden als Material für die Herstellung des Drehrohres 1 und/oder der Mischelemente 3 und/oder das bzw. die Verstärkungselemente 8 ferritische oder ferritisch-austenitische Stähle mit gutem Korrosions- und Hochtemperaturverhalten verwendet.As far as the
Des weiteren weist das erfindungsgemäße Drehrohr 1 vorteilhafterweise Einlaß- und Auslaßeinrichtungen zum Einführen und Auslassen sowie Durchleiten von Gasen auf, beispielsweise zum Einleiten von Inertgasen für die Carbonisierungsphase bei der Aktivkohleherstellung und zum Einleiten von Oxidationsgasen für die Aktivierungsphase bei der Aktivkohleherstellung. Dies ist in den Figuren nicht dargestellt.Furthermore, the
Zu einer verbesserten Wartung des Innenraums 2 des Drehrohres 1 kann dieses in der Wandung des Drehrohres ein sogenanntes Mannloch aufweisen, welches dicht mit dem Drehrohr 1 verschließbar ist und so das Einsteigen von Wartungspersonal in den Innenraum 2 des Drehrohres 1 außerhalb des Betriebs ermöglicht. Dies ist in den Figuren ebenfalls nicht dargestellt. Auf diese Weise wird eine Wartung auch des Innenraums 2 des Drehrohres 1 auf einfache Weise gewährleistet.For improved maintenance of the
Wie zuvor beschrieben, wird das Drehrohr 1 nach der vorliegenden Erfindung insbesondere in Drehrohröfen zur Herstellung von Aktivkohle verwendet. Gegenstand der vorliegenden Erfindung ― gemäß einem zweiten Aspekt der vorliegenden Erfindung ― ist somit ein Drehrohrofen, welcher das zuvor beschriebene Drehrohr 1 nach der vorliegenden Erfindung aufweist.As described above, the
Weiterer Gegenstand der vorliegenden Erfindung - gemäß einem dritten Aspekt der Erfindung - ist die Verwendung eines wie zuvor beschriebenen Drehrohres 1 bzw. eines dieses Drehrohr 1 enthaltenen Drehrohrofens zur Herstellung von Aktivkohle. Wie im Einleitungsteil der vorliegenden Erfindung beschrieben, erfolgt die Herstellung der Aktivkohle im allgemeinen durch Carbonisierung (synonym auch als Pyrolyse, Schwelung oder Verkokung bezeichnet) und nachfolgende Aktivierung kohlenstoffhaltiger Ausgangsmaterialien, insbesondere organischer Polymere, so z. B. sulfonierter organischer Polymere (z. B. sulfonierter divinylbenzolvernetzter Polystyrole), welche in dem Drehrohr bzw. Drehrohrofen nach der vorliegenden Erfindung carbonisiert und nachfolgend aktiviert werden. Dabei wird die Carbonisierung im allgemeinen bei Temperaturen von 100 °C bis 750 °C, insbesondere 150 °C bis 650 °C, vorzugsweise 200 °C bis 600 °C, durchgeführt, vorzugsweise unter inerter oder allenfalls leicht oxidierender Atmosphäre, wie im einleitenden Teil beschrieben. Dabei kann der Carbonisierung noch eine Stufe der Vorcarbonisierung bzw. Vorschwelung vorgeschaltet sein. Die Aktivierung wird dagegen im allgemeinen bei Temperaturen von 700 °C bis 1.200 °C, insbesondere 800 °C bis 1.100°C, vorzugsweise 850 °C bis 1.000 °C, durchgeführt. Die Carbonisierung wird ― wie im einleitenden Teil beschrieben ― im allgemeinen unter kontrolliert bzw. selektiv oxidierenden Bedingungen, insbesondere unter kontrolliert oxidierender Atmosphäre, durchgeführt. Ais geeignete Ausgangspolymere der vorgenannten Art sind insbesondere Ionenaustauscherharze (z. B. Kationenaustauscherharze bzw. saure Ionenaustauscherharze, vorzugsweise mit Sulfonsäuregruppen, so z. B. Kationenaustauscherharze auf Basis sulfonierter Styrol/Divinylbenzol-Copolymere) bzw. deren Vorstufen (d. h. die unsulfonierten Ionenaustauscherharze, welche vor oder bei der Carbonisierung noch mit einem geeigneten Sulfonierungsmittel, wie z. B. Schwefelsäure und/oder Oleum, sulfoniert werden müssen) zu nennen. Für weitere diesbezügliche Einzelheiten kann auf obige Ausführungen im einleitenden Teil verwiesen werden.Another object of the present invention - according to a third aspect of the invention - is the use of a
Die außenseitige Anbringung des bzw. der Verstärkungselemente bewirkt, daß die mechanische Stabilität bzw. die Formstabilität des Drehrohres im Betriebszustand, insbesondere auch unter extremen Bedingungen (wie sie z. B. bei der Aktivkohleherstellung auftreten), beträchtlich verbessert wird. Auf diese Weise wird ein Drehrohr geschaffen, welches mechanischen Deformationen besser widerstehen kann und resistenter auch gegenüber starken Druckdifferenzen und Druckschwankungen ist und somit auch unter Betriebsbedingungen formstabil ist. Das erfindungsgemäße Drehrohr weist folglich eine verbesserte Lebensdauer mit verringerter Tendenz zur vorzeitigen Materialermüdung auf. Auch sind infolgedessen die Prozeßführung und Prozeßkontrolle erleichtert.The external attachment of the reinforcing elements or causes the mechanical stability or the dimensional stability of the rotary tube in the operating state, especially under extreme conditions (such as occur in the activated carbon production, for example), is considerably improved. In this way, a rotary tube is provided which can better resist mechanical deformation and is more resistant to strong pressure differences and pressure fluctuations and thus is dimensionally stable under operating conditions. The rotary tube according to the invention consequently has an improved service life with a reduced tendency for premature material fatigue. As a result, the process control and process control are facilitated.
Das Drehrohr bzw. der Drehrohrofen nach der vorliegenden Erfindung ermöglicht die Herstellung von Aktivkohle ausgehend von geeigneten kohlenstoffhaltigen Ausgangsmaterialien durch Carbonisierung und nachfolgende Aktivierung in einer einzigen Apparatur unter relativ leichter Handhabung. Durch die außenseitige Verschweißung der Mischelemente wird ein leicht zu wartendes, wenig reparaturanfälliges System bereitgestellt, welches geeignet ist, sowohl den extrem korrosiven Bedingungen der Carbonisierungsphase als auch den Hochtemperaturbedingungen der Aktivierungsphase standzuhalten; die außenseitige Verschweißung der Mischelemente ermöglicht die Verwendung von Verschweißungsmaterialien (= Schweißmaterialien bzw. Schweißgut), die für die Verschweißung optimal geeignet sind, aber für eine innenseitige Verschweißung nicht ohne weiters Anwendung finden könnten, da sie den korrosiven Hochtemperaturbedingungen im Inneren des Drehrohrofens während des Betriebszustandes nicht ohne weiteres auf Dauer standhalten würden.The rotary kiln of the present invention enables the production of activated carbon from suitable carbonaceous raw materials by carbonization and subsequent activation in a single apparatus with relatively easy handling. Outer welding of the mixing elements provides an easy-to-maintain, low-repair-prone system capable of withstanding both the extremely corrosive conditions of the carbonation phase and the high temperature conditions of the activation phase; the external welding of the mixing elements allows the use of welding materials (= welding materials) which are optimally suited for welding, but which could not easily be used for internal welding, as they corrode the high temperature conditions inside the rotary kiln would not readily withstand during the operating state in the long term.
Weitere Vorteile, Ausgestaltungen, Abwandlungen, Variationen und Eigenschaften der vorliegenden Erfindung sind für den Fachmann beim Lesen der Beschreibung ohne weiteres ersichtlich und verständlich, ohne daß er hierbei den Rahmen der vorliegenden Erfindung verläßt.Further advantages, embodiments, modifications, variations and features of the present invention will be readily apparent to and understood by those skilled in the art upon reading the description, without thereby departing from the scope of the present invention.
Claims (13)
- A rotary tube (1) for a rotary tube kiln for the production of activated carbon, wherein the rotary tube (1) is equipped on the exterior thereof with at least one reinforcing element (8) extending completely across the circumference of the rotary tube (1) for stabilizing the rotary tube (1) in the operating state,
characterized in that
the reinforcing element (8) consists of the same material as the rotary tube (1), wherein the reinforcing element (8) and the rotary tube (1) both consist of highly temperature-resistant steel,
the reinforcing element (8), along with the rotary tube (1), is welded via a weld joint (9) extending along a contact line of the reinforcing element (8) together with the rotary tube (1) in a manner free of interruptions, and
mixing elements (3) for the agitation and/or mixing of the charged goods (4) are arranged in the interior (2) of the rotary tube (1), wherein the rotary tube (1) comprises through holes (5) for receiving fastening sections (6) of the mixing elements (3), and the fastening sections (6) are welded onto the exterior of the rotary tube (1). - The rotary tube according to claim 1, characterized in that the reinforcing element (8) is embodied such that the reinforcing element (8) extends peripherally about the rotary tube (1), in particular perpendicular or at an angle to the rotary axis of the rotary tube (1).
- The rotary tube according to claims 1 or 2, characterized in that the reinforcing element (8) is embodied in the shape of ribs, annularly, in particular as an annular flange, or in the shape of a screw line.
- The rotary tube according to one of the previous claims, characterized in that the reinforcing element (8) extends axially along the rotary tube (1), in particular across the entire length thereof.
- The rotary tube according to one of the previous claims, characterized in that the weld joint (9) comprises at least two welded layers (9a, 9b).
- The rotary tube according to one of the previous claims, characterized in that the mixing elements (3) engage radially into the rotary tube (1), and are welded to the exterior of the rotary tube (1).
- The rotary tube according to one of the previous claims, characterized in that the reinforcing elements (8) is connected, in particular welded, to the exterior of the at least one fastening section (6), in particular wherein the fastening sections (6) of the mixing elements (3) project on the exterior side.
- The rotary tube according to one of the previous claims, characterized in that the reinforcing element (8) comprises at least one recess (10) for receiving a fastening section (6) of a mixing element (3).
- The rotary tube according to one of the previous claims, characterized in that the exterior welding of the fastening sections (6) of the mixing elements (3) to the rotary tube (1) is carried out via a welding section (7).
- The rotary tube according to one of the previous claims, characterized in that mixing elements (3) are embodied in the manner of vanes or plates.
- A rotary tube kiln, in particular for the production of activated carbon, comprising a rotary tube (1) according to claims 1 to 10.
- Use of a rotary tube according to claims 1 to 10 or of a rotary tube kiln according to claim 11 for the production of activated carbon, wherein the production of activated carbon is carried out by means of carbonation and subsequent activation of base materials containing carbon.
- Use according to claim 12, characterized in that the carbonation is carried out at temperatures ranging from 100 to 750 °C, in particular 150 to 650 °C, preferably 200 to 600 °C, and/or that the activation is carried out at temperatures ranging from 700 to 1,200 °C, in particular 800 to 1,100 °C, preferably 850 to 1,000 °C.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005035907 | 2005-07-28 | ||
DE102005036607A DE102005036607A1 (en) | 2005-07-28 | 2005-08-01 | Rotary kiln for the production of activated carbon |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1748269A2 EP1748269A2 (en) | 2007-01-31 |
EP1748269A3 EP1748269A3 (en) | 2009-07-29 |
EP1748269B1 true EP1748269B1 (en) | 2012-09-12 |
Family
ID=37311867
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06013903A Active EP1748269B1 (en) | 2005-07-28 | 2006-07-05 | Rotary furnace for manufacturing activated carbon |
Country Status (4)
Country | Link |
---|---|
US (1) | US7866977B2 (en) |
EP (1) | EP1748269B1 (en) |
JP (1) | JP4688039B2 (en) |
DE (1) | DE102005036607A1 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005036607A1 (en) | 2005-07-28 | 2007-02-08 | BLüCHER GMBH | Rotary kiln for the production of activated carbon |
EP1903292B1 (en) * | 2006-09-19 | 2011-11-16 | Blücher GmbH | Rotary furnace for manufacturing active carbon using modified rotary pipe geometry |
ITTO20070084A1 (en) * | 2007-02-06 | 2008-08-07 | K & E Srl | RADIAL MIXING DEVICES FOR ROLLING INCLINED REACTORS. |
JP5110951B2 (en) * | 2007-04-27 | 2012-12-26 | 三井造船株式会社 | Tire support structure in a horizontal rotary dryer. |
AU2008280722B2 (en) * | 2007-07-25 | 2013-11-21 | Qihui Lian | Disposal method for entirely recycling solid refuse |
DE102009032810A1 (en) | 2009-07-10 | 2011-01-13 | BLüCHER GMBH | Plant and process for the production of activated carbon |
DE102013009961A1 (en) * | 2013-05-17 | 2014-12-04 | BLüCHER GMBH | Rotary kiln and rotary kiln for the production of activated carbon |
JP6245743B2 (en) | 2013-12-06 | 2017-12-20 | 三菱重工業株式会社 | Coal deactivation processing equipment |
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DD62256A1 (en) * | 1967-10-06 | 1968-06-05 | Werner Schultz | Method and device for generating a favorable heat transfer between the heat source or the furnace shell and the kiln inside a rotary kiln |
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DE102005036607A1 (en) | 2005-07-28 | 2007-02-08 | BLüCHER GMBH | Rotary kiln for the production of activated carbon |
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-
2005
- 2005-08-01 DE DE102005036607A patent/DE102005036607A1/en not_active Ceased
-
2006
- 2006-07-05 EP EP06013903A patent/EP1748269B1/en active Active
- 2006-07-27 US US11/494,110 patent/US7866977B2/en active Active
- 2006-07-28 JP JP2006206213A patent/JP4688039B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
US20070031772A1 (en) | 2007-02-08 |
DE102005036607A1 (en) | 2007-02-08 |
JP2007031275A (en) | 2007-02-08 |
EP1748269A3 (en) | 2009-07-29 |
JP4688039B2 (en) | 2011-05-25 |
EP1748269A2 (en) | 2007-01-31 |
US7866977B2 (en) | 2011-01-11 |
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