CN105195237A - Dipping drum and catalyst production device - Google Patents
Dipping drum and catalyst production device Download PDFInfo
- Publication number
- CN105195237A CN105195237A CN201410255265.6A CN201410255265A CN105195237A CN 105195237 A CN105195237 A CN 105195237A CN 201410255265 A CN201410255265 A CN 201410255265A CN 105195237 A CN105195237 A CN 105195237A
- Authority
- CN
- China
- Prior art keywords
- rotary drum
- dipping
- drum body
- carrier
- shower nozzle
- 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.)
- Pending
Links
Abstract
The invention discloses a dipping drum which comprises a drum body (1) used for carrying a catalyst carrier. The drum body is connected with a drive shaft (2) used for driving the drum body to rotate. The joint of the drive shaft and the drum body is provided with a discharge opening for discharging evaporating gas in the drum body. The invention further provides a catalyst production device comprising a dipping drum device used for dipping active components of a dipping solution on the carrier, and a quick drying device used for drying the dipped carrier. The dipping drum device comprises the dipping drum. By means of the dipping drum and the catalyst production device, loss of the dipping solution can be reduced, and besides, the quality of catalyst products is more stable.
Description
Technical field
The present invention relates to field of catalyst preparation, particularly, relate to a kind of dipping rotary drum and Catalyst Production equipment.
Background technology
In catalyst preparing and production process, there is multiple production method, as infusion process, roll coating process, the precipitation method, mixing method, ion-exchange, gas phase synthesis method etc.Wherein infusion process is a kind of comparatively conventional method.
In infusion process, it will activity component impregnation to carrier be wherein most important step.Traditional impregnation of catalyst carriers equipment mainly contains impregnating autoclave, dipping hanging basket, dipping guipure, dipping cylinder, dipping rotary drum, dipping bowling machine etc.Fluidized bed immersion is applicable to the dipping of porous carrier, but there is finished catalyst yield low (80 ~ 90%), easily caking, the problem such as uneven.
Use dipping rotary drum when flooding in prior art, carrier is placed in rotary drum, and dipping solution is imported in rotary drum to make solution can impregnated carrier.The lead-in mode of solution directly makes liquid flow in rotary drum.Be understandable that in this case, only have that to import carrier hole saturated or import the imbibition requirement that excessive dipping solution could meet carrier, i.e. saturated dipping even supersaturation dipping.So not only can cause the waste of a large amount of solution, also cause the requirement that cannot meet production active component heterogeneous catalyst.In addition, in impregnation technology, especially in the impregnation technology preparing heterogeneous catalyst, need constantly to remove the boil-off gas (being generally water) produced because of heating, otherwise can be unfavorable to dipping process.But dipping rotary drum of the prior art is closed device, usually need to adopt the method vacuumized to remove boil-off gas.And vacuumize the dipping solution taking a lot of atomizations away, not only cause the loss of a large amount of dipping solutions, the metering in catalyst preparation process also can be caused inaccurate difficult with control.Further, the closed state flooding rotary drum also can cause difficulty to the importing of liquid.
Therefore, impregnating equipment of the prior art haves much room for improvement.
Summary of the invention
The object of this invention is to provide a kind of dipping rotary drum and Catalyst Production equipment, in order to reduce the loss of dipping solution, and realize the dipping and the active component distribution in the catalyst that control active component flexibly, thus make the quality of catalyst prod more stable.
To achieve these goals, the invention provides a kind of dipping rotary drum, comprise the rotary drum body for bearing catalyst carrier, rotary drum body is connected with the driving shaft for driving rotary drum body to rotate, wherein, at the connecting portion of driving shaft and rotary drum body, offer the floss hole for discharging the boil-off gas in rotary drum body.
Preferably, rotary drum body is taper or the biconial sharing same cone bottom surface, and driving shaft is connected to position bottom taper or diconical cone.
Preferably, dipping rotary drum also comprises the pedestal for supporting rotary drum body, driving shaft is connected to pedestal rotationally, wherein, be connected to each other by the link of umbrella frame shape between the outer wall of driving shaft and rotary drum body, and floss hole is opened in being enclosed in the region that formed by the position be connected with link on rotary drum body.
Preferably, the solution that dipping rotary drum also comprises for adding dipping solution in rotary drum body imports unit, and solution importing unit comprises the sprayer be arranged in rotary drum body.
Preferably, shower nozzle is arranged on the diconical position near at least one vertex of a cone, and shower nozzle is adjustable to the distance of diconical inwall.
Preferably, shower nozzle is to regulate the pressure nozzle of spray angle, two phase flow shower nozzle, ultrasonic nozzle and/or static nozzle.
Preferably, the diameter of the drop that shower nozzle sprays is 1 μm to 1000 μm, is preferably 10 μm to 500 μm, more preferably 20 μm to 200 μm.
Preferably, link is formed by many reinforcement welding.
Preferably, the internal face of rotary drum body is provided with lifting blade, lifting blade is not more than 300mm relative to the height of projection of the internal face of rotary drum body, is preferably not more than 150mm, more preferably 10mm to 100mm.
On the other hand, the present invention also provides a kind of Catalyst Production equipment, comprise for by the activity component impregnation of dipping solution to the dipping drum device on carrier, and for the carrier through dipping is carried out dry rapid drying device, this dipping drum device comprises above-mentioned dipping rotary drum.
Preferably, dipping rotary drum also comprises the pedestal for supporting rotary drum body, driving shaft is connected to pedestal rotationally, wherein, be connected to each other by the link of umbrella frame shape between the outer wall of driving shaft and rotary drum body, and floss hole is opened in being enclosed in the region that formed by the position be connected with link on rotary drum body.
Preferably, the solution that dipping rotary drum also comprises for adding dipping solution in rotary drum body imports unit, and solution importing unit comprises the sprayer be arranged in rotary drum body.
Preferably, dipping drum device also comprises the carrier feed unit for adding carrier in rotary drum body, and for carrying the fluid delivery unit of dipping solution, wherein, the output of carrier feed unit is removably connected with the vertex of a cone position of rotary drum body, and the output of fluid delivery unit is connected to the input that solution imports unit.
Preferably, rapid drying device comprises dry zone and the distributing device for guiding to through the carrier of dipping in rotary drum body on dry zone, and the carrier through flooding forms the bed of material of 0.2cm to 5cm on dry zone by distributing device, wherein, the width of dry zone is 0.5m to 3m, the baking temperature of dry zone is 20 DEG C to 600 DEG C, is preferably 100 DEG C to 500 DEG C, more preferably 120 DEG C to 400 DEG C.
Preferably, rotary drum body is biconial, and this diconical first vertex of a cone is removably connected with the output of carrier feed unit, and when first vertex of a cone is connected with the output of carrier feed unit, diconical second vertex of a cone is just to the arrival end of distributing device.
Preferably, sprayer comprises multiple shower nozzle, and shower nozzle is arranged on the diconical position near at least one vertex of a cone, and shower nozzle is adjustable to the distance of diconical inwall.
Preferably, the diameter of the drop that shower nozzle sprays is 1 μm to 1000 μm, is preferably 10 μm to 500 μm, more preferably 20 μm to 200 μm.
Preferably, link is formed by many reinforcement welding.
Preferably, the internal face of rotary drum body is provided with lifting blade, lifting blade is not more than 300mm relative to the height of projection of the internal face of rotary drum body, is preferably not more than 150mm, more preferably 10mm to 100mm.
By technique scheme, the rotary drum body of dipping rotary drum of the present invention is arranged the floss hole for discharging boil-off gas.By arranging these floss holes, the mode that vacuumizes can be re-used to extract boil-off gas.By this, the loss of dipping solution can be greatly reduced on the one hand, investment and the maintenance cost of vaccum-pumping equipment can also be saved on the other hand.In Catalyst Production equipment, use above-mentioned dipping rotary drum, the dipping and the active component distribution in the catalyst that control active component flexibly can be realized, thus make the quality of catalyst prod more stable.
Other features and advantages of the present invention are described in detail in detailed description of the invention part subsequently.
Accompanying drawing explanation
Accompanying drawing is used to provide a further understanding of the present invention, and forms a part for description, is used from explanation the present invention, but is not construed as limiting the invention with detailed description of the invention one below.In the accompanying drawings:
Fig. 1 is the structural representation according to dipping rotary drum of the present invention;
Fig. 2 is the structural representation of Catalyst Production equipment of the present invention.
Description of reference numerals
1 rotary drum body 11 first vertex of a cone 12 second vertex of a cone
2 driving shaft 3 pedestal 4 links
5 nozzle 6 motor 7 reductors
8 carrier feed unit 9 fluid delivery unit
101 dry zone 102 distributing devices
Detailed description of the invention
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is described in detail.Should be understood that, detailed description of the invention described herein, only for instruction and explanation of the present invention, is not limited to the present invention.
With reference to figure 1, the invention provides a kind of dipping rotary drum.This dipping rotary drum comprises rotary drum body 1.In the impregnation steps of the technique of Kaolinite Preparation of Catalyst, catalyst carrier is placed in rotary drum body 1.As shown in fig. 1, flood rotary drum and also comprise motor 6 for driving rotary drum body 1 to rotate and reductor 7.Rely on gear, hinge and/or belt transmission between motor 6 and reductor 7, and the output of reductor 7 is connected with the driving shaft 2 for exporting rotating torque.Dipping rotary drum also comprises the pedestal 3 for supporting rotary drum body 1, and driving shaft 2 can be connected to pedestal 3 rotationally by the structure of such as bearing.When motor 6 and reductor 7 unlatching make driving shaft 2 rotate, rotating torque can be passed to rotary drum body 1 by driving shaft 2, thus the carrier in rotary drum body 1 is stirred, to reach good dipping effect.According to embodiments of the invention, the velocity of rotation of rotary drum body 1 can select 0.5 turn/min ~ 100 turn/min, is preferably 5 turns/min ~ 60 turn/min, more preferably 10 turns/min ~ 50 turn/min.At these speeds, carrier stirs evenly, good fluidity.Many experiments data show, during lower than this rotating speed, carrier to stir effect bad, during higher than this rotating speed, catalyst particle attrition, efflorescence can be caused.
Continue with reference to figure 1, according to embodiments of the invention, the solution that dipping rotary drum also comprises for adding dipping solution in rotary drum body 1 imports unit.In the impregnation steps of the technique of Kaolinite Preparation of Catalyst, realize activity component impregnation on carrier by adding dipping solution in rotary drum body 1.According to embodiments of the invention, solution importing unit comprises the sprayer on the inwall being connected to rotary drum body 1.Rotated and the cooperatively interacting of spray structure by rotary drum body 1, dipping solution can be sprayed onto in the inner space of rotary drum body 1 quickly and evenly with the form of drop, thus make dipping solution be impregnated into carrier quickly and evenly.By this, saturated dipping or supersaturation dipping can be carried out on the one hand, thus the waste of dipping solution can be greatly reduced; Pickling efficiency can also be improved on the other hand.
In more detail, according to embodiments of the invention, sprayer comprises multiple shower nozzle 5 that can regulate spray angle.These shower nozzles 5 can carry out horizontal and vertical ordered arrangement according to the distribution of carrier in rotary drum body 1, thus ensure that the liquid of ejection can fully receive by loaded body.The spray angle of shower nozzle 5 can be controlled by automaton.According to embodiments of the invention, the selection of shower nozzle can need to carry out according to the preparation of catalyst, such as but not limited to, can selection pressure shower nozzle, two phase flow shower nozzle, ultrasonic nozzle and/or static nozzle.In order to reduce costs, can pressure nozzle that preferably use cost is lower.According to embodiments of the invention, the diameter of the drop that shower nozzle sprays is chosen as 1 μm to 1000 μm, can be preferably 10 μm to 500 μm, can more preferably 20 μm to 200 μm.Such atomized drop, can be of a size of the carrier of 1mm ~ 5mm by multiple-contact, make substrate monolith appearance uniform, and in each carrier, active component present non-uniform Distribution.In addition, according to embodiments of the invention, when measuring the size of drop, drop can be sprayed at and scribble on the glass plate of wax material, then amplify 100 times under the microscope, measure the diameter of drop.
Further, according to embodiments of the invention, the internal face of rotary drum body 1 is provided with lifting blade.Thus when rotary drum body 1 rotates, carrier can be kicked up certain height under the carrying in lifting portion.By this, carrier can be realized in rotary drum body 1, carry out more effective stirring, thus promote the contact of carrier and dipping solution, to increase the uniformity of catalyst preparing and overall uniformity.According to embodiments of the invention, lifting blade can distribute in length and breadth thus form grille-like on the inwall of rotary drum body 1.Preferably, grid can be triangle, rectangle or trapezoidal.More preferably, grid is rectangle.Further, according to embodiments of the invention, lifting blade is not more than 300mm relative to the height of projection of the internal face of rotary drum body 1, is preferably not more than 150mm, more preferably 10mm to 100mm.Many experiments data show, and when being less than this height of projection, the carrying capacity of lifting blade is not enough, when being greater than this height of projection, can cause catalyst particle attrition, efflorescence.In addition, the inwall of rotary drum body 1 and the material of lifting blade can be preferably stainless steel.
Still with reference to figure 1, according to embodiments of the invention, dipping rotary drum also comprises intensification unit for heating drum body 1, to ensure intensification in dipping process and insulation.Rotary drum body 1 can produce boil-off gas after being warmed unit heating.According to embodiments of the invention, rotary drum body 1 is provided with the floss hole for discharging these boil-off gas.By arranging these floss holes, the mode that vacuumizes can be re-used to extract boil-off gas.By this, the loss of dipping solution can be greatly reduced on the one hand, investment and the maintenance cost of vaccum-pumping equipment can also be saved on the other hand.
In more detail, according to embodiments of the invention, the shape of rotary drum body 1 can be the shape such as cydariform or ellipse roughly.Preferably, the shape of rotary drum body 1 can be set to the biconial shown in Fig. 1.This biconial can be the biconial of shared same cone bottom surface, also can be the biconial not sharing same cone bottom surface.The driving shaft 2 rotated for driving rotary drum body 1 can be connected to the side of rotary drum body 1.That is, position, diconical cone bottom is connected to as illustrated in figure 1.Like this, when driving shaft 2 drives rotary drum body 1 to rotate, due to the effect of centrifugal force, the carrier carried in rotary drum body 1 can move towards the cone top part displacement away from driving shaft 1.According to embodiments of the invention, the floss hole for discharging boil-off gas can be opened in the connecting portion of driving shaft 2 and rotary drum body 1.As mentioned above, carrier can move towards cone top part displacement away from driving shaft 1 under the influence of centrifugal force, and that is carrier can move towards the direction away from floss hole, and carrier therefore can be avoided to leak from floss hole.In addition, according to embodiments of the invention, shower nozzle 5 is arranged on the diconical position near at least one vertex of a cone diconical.That is, shower nozzle 5 can be arranged in one of them taper diconical, and the position of the vertex of a cone of this taper close; Also can be separately positioned in two tapers, and respectively near the position of the vertex of a cone of two tapers.And in the present embodiment, the distance of the inwall of shower nozzle 5 to taper is adjustable.That is, shower nozzle 5 can move along the radial direction of taper.Above, by shower nozzle 5 being arranged on the position at the top near taper, can make the position that shower nozzle 5 can be concentrated closer to carrier; By regulating shower nozzle 5 relative to the spacing of conical inboard wall, the adjustment of the jet length of shower nozzle 5 can be realized, thus ensure that the dipping solution of predetermined amount can be ejected on carrier; By controlling the sprinkling direction of shower nozzle 5, shower nozzle 5 can be controlled better and be sprayed onto effective spray area on carrier.
More specifically, according to embodiments of the invention, the link 4 by umbrella frame shape between the outer wall of driving shaft 2 and rotary drum body 1 is connected to each other.Wherein, as shown in fig. 1, the top of the gathering of link 4 is connected to driving shaft 2, and one end strutted of link 4 is connected to the outside wall surface of rotary drum body 1.Like this, in the outside wall surface of rotary drum body 1, can enclose by the position be connected with link 4 region forming a similar round.According to embodiments of the invention, can be opened in the region of this similar round for the floss hole discharging boil-off gas.Further, link 4 can be formed by many reinforcement welding, so that draw materials and reduce costs.Further, link 4 can be connected on the internal face of rotary drum body 1 by welding or cold rolling mode.Like this, can drain from the spacing (spacing between each bar umbrella frame of also i.e. umbrella frame shape structure) between reinforcing bar from the boil-off gas of floss hole discharge.
By said structure, the sprinkling of dipping solution can be implemented in drum rotating process, and by boil-off gas Natural excrement in dipping process, thus meet the working condition of catalyst particularly heterogeneous catalyst preferably.In addition, according to embodiments of the invention, shower nozzle 5 is set to towards diconical vertex of a cone position.The distance of shower nozzle distance material is relevant with operating condition with the selection of shower nozzle 5.Shower nozzle 5 towards regulating, specifically can regulate according to the direction of rotary drum body 1 and speed, to ensure that spraying liquid is effectively sprayed at the surface of material.In rotary drum body 1 rotary course, carrier concentrates on vertex of a cone position because of the effect of centrifugal force, and shower nozzle 5 arranges towards vertex of a cone position and can ensure that dipping solution can be sprayed onto on carrier efficiently.
On the other hand, with reference to figure 2, the present invention also provides a kind of Catalyst Production equipment.This equipment comprises dipping drum device and rapid drying device.Wherein, dipping drum device be used for by the activity component impregnation of dipping solution to carrier, rapid drying device be used for by through dipping carrier carry out drying.
According to embodiments of the invention, dipping drum device comprises above-mentioned dipping rotary drum, also comprises the carrier feed unit 8 for adding carrier in rotary drum body 1, and for carrying the fluid delivery unit 9 of dipping solution in rotary drum body 1.Wherein, carrier feed unit 8 comprises the hopper for holding carrier and the control valve for controlling charging rate.According to embodiments of the invention, the outlet of control valve is the output of carrier feed unit 8, and this output is removably connected to the vertex of a cone position of rotary drum body 1.Further, according to embodiments of the invention, the inlet amount of carrier is determined according to the amount of solution, the speed of spraying, the rotating speed of rotary drum body 1 and default dip time.By control valve, the inlet amount of carrier is controlled to criticize for 20kg/ criticizes-1000kg/, be preferably 50kg/ and criticize-800kg/ and criticize, more preferably 100kg/ criticizes-300kg/ and criticizes.Further, the inlet amount of carrier can regulate according to the size of equipment, to reach the object of effectively producing smoothly.
According to embodiments of the invention, the output of fluid delivery unit 9 is connected to the input that solution imports unit, thus is provided for the dipping solution of sprinkling to shower nozzle 5.Wherein, fluid delivery unit 9 comprises solution storage tank, constant pressure pump and control valve.According to embodiments of the invention, control valve may be used for the fluid pressure and the mist flow that control shower nozzle 5.The fluid pressure of shower nozzle 5 may be controlled to 0.05MPa-10.0MPa, is preferably 0.1MPa-5.0MPa, more preferably 0.2MPa-2.0MPa.According to the difference of shower nozzle, corresponding atomization condition can be selected, reach good atomizing effect.Droplet size is relevant with the size of pressure, and the requirement of granule carrier to atomizing effect is higher.Mist flow may be controlled to 0.1L/min-10.0L/min, is preferably 0.2L/min-8.0L/min, more preferably 0.5L/min-5.0L/min.According to the number that output and carrier add, the flow of matching liquid.
According to above-mentioned, because the rotating speed of rotary drum body 1, the system pressure of sprayer and flow can be controlled by automatics, therefore, production equipment of the present invention can realize the dipping and the active component distribution in the catalyst that control active component flexibly.Thereby eliminate traditional infusion process and produce the equipment of catalyst and the shortcoming of device, solve the change of impregnating equipment and technique and the upgrading of catalyst prod in catalyst preparation process.Especially, in the process for producing of heterogeneous catalyst, the catalyst prod that quality is more stable can be obtained.
Continue with reference to figure 2, according to embodiments of the invention, rapid drying device comprises dry zone 101 and distributing device 102.Wherein, distributing device 102 can be arranged on the top of dry zone 101, for the carrier through dipping in rotary drum body 1 is guided to dry zone 101.According to embodiments of the invention, distributing device 102 can be arranged to infundibulate, and the outlet of this funnel can be arranged on directly over dry zone 102.In a preferred embodiment, rotary drum body 1 is biconial, and this diconical first vertex of a cone 11 is removably connected with the output of carrier feed unit 8.Further, when first vertex of a cone 11 is connected with the output of carrier feed unit 8, diconical second vertex of a cone 12 is just to the arrival end of distributing device 102.That is, when discharging discharging, first vertex of a cone 11 (being now relatively in top) can be connected with the outlet of the control valve of carrier feed unit 8, below now second vertex of a cone 12 is relatively in and just to the entrance of distributing device 102.Like this, discharging and discharging can complete in an operation, thus increase work efficiency.Be understandable that, because second vertex of a cone 12 is now in the bottommost of rotary drum body 1, and the inferior pyramidal of rotary drum body 1 is infundibulate, and therefore carrier can draw off easily from second vertex of a cone 12.
According to embodiments of the invention, the width of dry zone 101 is 0.5m to 3m, is preferably 0.5m-2.0m.By the control of width, both can uniform distribution be reached, again can the object of uniform drying.The baking temperature of dry zone 101 is 50 DEG C to 600 DEG C, is preferably 100 DEG C to 500 DEG C, more preferably 120 DEG C to 400 DEG C, thus completes the quick-drying object of catalyst.Many experiments data show, if baking temperature is not suitable for, can cause deliquescence, cause moisture to turn back in catalyst, affect the quality of finished product.In addition, according to embodiments of the invention, on dry zone 101, to be formed the bed of material of 0.2cm to 5.0cm through the carrier of dipping by distributing device 102, be preferably the bed of material of 0.5cm to 3.0cm, then be preferably the bed of material of 0.5cm to 2.0cm.The control of thickness of feed layer, can make catalyst fully dry, avoids causing because the bed of material is too thick moisture adsorbing and destroying the performance of catalyst in the catalyst.In addition, if thickness of feed layer is unreasonable, the moisture inner layer on top layer can be caused to absorb and lose product qualified rate.
Below the preferred embodiment of the present invention is described in detail by reference to the accompanying drawings; but; the present invention is not limited to the detail in above-mentioned embodiment; within the scope of technical conceive of the present invention; can carry out multiple simple variant to technical scheme of the present invention, these simple variant all belong to protection scope of the present invention.
It should be noted that in addition, each the concrete technical characteristic described in above-mentioned detailed description of the invention, in reconcilable situation, can be combined by any suitable mode.In order to avoid unnecessary repetition, the present invention illustrates no longer separately to various possible combination.
In addition, also can be combined between various different embodiment of the present invention, as long as it is without prejudice to thought of the present invention, it should be considered as content disclosed in this invention equally.
Claims (19)
1. a dipping rotary drum, comprise the rotary drum body (1) for bearing catalyst carrier, described rotary drum body (1) is connected with the driving shaft (2) for driving described rotary drum body (1) to rotate, it is characterized in that, at the connecting portion of described driving shaft (2) with described rotary drum body (1), offer the floss hole for discharging the boil-off gas in described rotary drum body (1).
2. dipping rotary drum according to claim 1, it is characterized in that, described rotary drum body (1) is taper or the biconial sharing same cone bottom surface, and described driving shaft (2) is connected to position bottom described taper or diconical cone.
3. dipping rotary drum according to claim 2, it is characterized in that, described dipping rotary drum also comprises the pedestal (3) for supporting described rotary drum body (1), and described driving shaft (2) is connected to described pedestal (3) rotationally
Wherein, be connected to each other by the link (4) of umbrella frame shape between the outer wall of described driving shaft (2) and described rotary drum body (1), and described floss hole is opened in being enclosed in the region that formed by the position be connected with described link (4) on described rotary drum body (1).
4. the dipping rotary drum according to Claims 2 or 3, it is characterized in that, the solution that described dipping rotary drum also comprises for adding dipping solution in described rotary drum body (1) imports unit, and described solution importing unit comprises the sprayer be arranged in described rotary drum body (1).
5. dipping rotary drum according to claim 4, is characterized in that, described shower nozzle (5) is arranged on the described diconical position near at least one vertex of a cone, and described shower nozzle (5) is adjustable to the distance of described diconical inwall.
6. dipping rotary drum according to claim 5, is characterized in that, described shower nozzle (5) is to regulate the pressure nozzle of spray angle, two phase flow shower nozzle, ultrasonic nozzle and/or static nozzle.
7. dipping rotary drum according to claim 6, is characterized in that, the diameter of the drop that described shower nozzle (5) sprays is 1 μm to 1000 μm, is preferably 10 μm to 500 μm, more preferably 20 μm to 200 μm.
8. dipping rotary drum according to claim 3, is characterized in that, described link (4) is formed by many reinforcement welding.
9. according to the dipping rotary drum in claim 1-3 described in any one, it is characterized in that, the internal face of described rotary drum body (1) is provided with lifting blade, described lifting blade is not more than 300mm relative to the height of projection of the internal face of described rotary drum body (1), preferably be not more than 150mm, more preferably 10mm to 100mm.
10. a Catalyst Production equipment, comprise for by the activity component impregnation of dipping solution to the dipping drum device on carrier, and for the carrier through dipping is carried out dry rapid drying device, it is characterized in that, described dipping drum device comprises dipping rotary drum according to claim 1.
11. Catalyst Production equipment according to claim 10, it is characterized in that, described dipping rotary drum also comprises the pedestal (3) for supporting described rotary drum body (1), and described driving shaft (2) is connected to described pedestal (3) rotationally
Wherein, be connected to each other by the link (4) of umbrella frame shape between the outer wall of described driving shaft (2) and described rotary drum body (1), and described floss hole is opened in being enclosed in the region that formed by the position be connected with described link (4) on described rotary drum body (1).
12. Catalyst Production equipment according to claim 11, it is characterized in that, the solution that described dipping rotary drum also comprises for adding dipping solution in described rotary drum body (1) imports unit, and described solution importing unit comprises the sprayer be arranged in described rotary drum body (1).
13. Catalyst Production equipment according to claim 12, it is characterized in that, described dipping drum device also comprises the carrier feed unit (8) for adding carrier in described rotary drum body (1), and for carrying the fluid delivery unit (9) of dipping solution
Wherein, the output of described carrier feed unit (8) is removably connected with the vertex of a cone position of described rotary drum body (1), and the output of described fluid delivery unit (9) is connected to the input that described solution imports unit.
14. Catalyst Production equipment according to claim 13, it is characterized in that, described rapid drying device comprises dry zone (101) and the distributing device (102) for guiding to through the carrier of dipping in described rotary drum body (1) on described dry zone (101), and the described carrier through dipping is by the bed of material of described distributing device (102) at described dry zone (101) upper formation 0.2cm to 5cm
Wherein, the width of described dry zone (101) is 0.5m to 3m, and the baking temperature of described dry zone (101) is 20 DEG C to 600 DEG C, is preferably 100 DEG C to 500 DEG C, more preferably 120 DEG C to 400 DEG C.
15. Catalyst Production equipment according to claim 13 or 14, it is characterized in that, described rotary drum body (1) is biconial, and this diconical first vertex of a cone (11) is removably connected with the output of described carrier feed unit (8), and
When described first vertex of a cone (11) is connected with the output of described carrier feed unit (8), described diconical second vertex of a cone (12) is just to the arrival end of described distributing device (102).
16. Catalyst Production equipment according to claim 15, it is characterized in that, described sprayer comprises multiple shower nozzle (5), described shower nozzle (5) is arranged on the described diconical position near at least one vertex of a cone, and described shower nozzle (5) is adjustable to the distance of described diconical inwall.
17. Catalyst Production equipment according to claim 16, is characterized in that, the diameter of the drop that described shower nozzle (5) sprays is 1 μm to 1000 μm, are preferably 10 μm to 500 μm, more preferably 20 μm to 200 μm.
18. Catalyst Production equipment according to claim 11, is characterized in that, described link (4) is formed by many reinforcement welding.
19. according to the Catalyst Production equipment in claim 10-14 described in any one, it is characterized in that, the internal face of described rotary drum body (1) is provided with lifting blade, described lifting blade is not more than 300mm relative to the height of projection of the internal face of described rotary drum body (1), preferably be not more than 150mm, more preferably 10mm to 100mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410255265.6A CN105195237A (en) | 2014-06-10 | 2014-06-10 | Dipping drum and catalyst production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410255265.6A CN105195237A (en) | 2014-06-10 | 2014-06-10 | Dipping drum and catalyst production device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105195237A true CN105195237A (en) | 2015-12-30 |
Family
ID=54943394
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410255265.6A Pending CN105195237A (en) | 2014-06-10 | 2014-06-10 | Dipping drum and catalyst production device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105195237A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108745423A (en) * | 2018-06-21 | 2018-11-06 | 江苏中科睿赛污染控制工程有限公司 | Honeycomb catalyst impregnates airing system |
| CN109562369A (en) * | 2016-05-30 | 2019-04-02 | Ifp 新能源公司 | The method for preparing selective hydrocatalyst |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87204630U (en) * | 1987-09-24 | 1988-07-27 | 中国石油化工总公司长岭炼油厂 | Spray impregnator for industrial use |
| CN202129081U (en) * | 2011-06-22 | 2012-02-01 | 淄博齐茂催化剂有限公司 | Equipment for impregnation of catalyst carriers |
| CN203550524U (en) * | 2013-10-29 | 2014-04-16 | 中国石油化工股份有限公司 | Double-frustum converter |
-
2014
- 2014-06-10 CN CN201410255265.6A patent/CN105195237A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87204630U (en) * | 1987-09-24 | 1988-07-27 | 中国石油化工总公司长岭炼油厂 | Spray impregnator for industrial use |
| CN202129081U (en) * | 2011-06-22 | 2012-02-01 | 淄博齐茂催化剂有限公司 | Equipment for impregnation of catalyst carriers |
| CN203550524U (en) * | 2013-10-29 | 2014-04-16 | 中国石油化工股份有限公司 | Double-frustum converter |
Non-Patent Citations (2)
| Title |
|---|
| 张继光主编: "《催化剂制备过程技术》", 31 October 2011, 中国石化出版社 * |
| 朱洪法，刘丽芝编: "《催化剂制备及应用技术》", 30 June 2011, 中国石化出版社 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109562369A (en) * | 2016-05-30 | 2019-04-02 | Ifp 新能源公司 | The method for preparing selective hydrocatalyst |
| CN109562369B (en) * | 2016-05-30 | 2022-09-20 | Ifp 新能源公司 | Process for preparing selective hydrogenation catalysts |
| CN108745423A (en) * | 2018-06-21 | 2018-11-06 | 江苏中科睿赛污染控制工程有限公司 | Honeycomb catalyst impregnates airing system |
| CN108745423B (en) * | 2018-06-21 | 2021-01-26 | 江苏中科睿赛环境工程有限公司 | Honeycomb catalyst dipping and airing system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205213343U (en) | Efficient coating machine uniform in coating | |
| CN111837568B (en) | Intelligent fertilizer applicator capable of automatically detecting soil fertility | |
| CN105195237A (en) | Dipping drum and catalyst production device | |
| RU2370937C1 (en) | Seed treater | |
| CN206909088U (en) | A kind of seed pelleting machine | |
| CN204147883U (en) | Dipping rotary drum and catalyst production equipment | |
| CN204093458U (en) | Dipping rotary drum and Catalyst Production equipment | |
| CN105268489A (en) | Dipping rotary drum and catalyst production equipment | |
| CN206355938U (en) | A kind of chemical liquid stock spraying opposite-flushing type fluid mixer | |
| CN105149013A (en) | Catalyst production technology | |
| CN202310517U (en) | Seed pelleting machine | |
| CN207022432U (en) | A kind of corn seed coating equipment in sugar production line | |
| CN216061310U (en) | Batch type double-function coating machine for coating and pelleting | |
| RU2380876C1 (en) | Seed treater of pneumatic-mechanical type | |
| CN209481506U (en) | Fertilizer coating device | |
| CN104368396A (en) | Catalyst preparation system | |
| CN206724579U (en) | A kind of drying device of high-efficiency and continuous | |
| CN216752701U (en) | A seed dressing device for pea seed | |
| CN208300246U (en) | A kind of efficient wheat seed-dressing device | |
| CN209128339U (en) | A kind of high tower granulator | |
| CN104368397A (en) | Preparation method for catalyst | |
| CN207685327U (en) | A kind of mixing machine improving balling ratio | |
| CN207591739U (en) | Powder solid, liquid mixer | |
| CN203678396U (en) | Catalyst preparation system | |
| CN216650443U (en) | Seed coating agent blanking device for seed coating machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20151230 |
|
| RJ01 | Rejection of invention patent application after publication |