CN206045962U - High tower grit blast crystal system - Google Patents
High tower grit blast crystal system Download PDFInfo
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- CN206045962U CN206045962U CN201620840009.8U CN201620840009U CN206045962U CN 206045962 U CN206045962 U CN 206045962U CN 201620840009 U CN201620840009 U CN 201620840009U CN 206045962 U CN206045962 U CN 206045962U
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- cooling tower
- tower
- wind
- solid granulates
- crystal system
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Abstract
This utility model discloses a kind of high tower grit blast crystal system, the high tower grit blast crystal system includes cooling tower, injection apparatus, centrifugal blower, fluid bed and discharging opening, the liquid thermal material in conveyance conduit is drawn to into cooling tower by injection apparatus, and by the liquid thermal material with liquid columnar shape from the top of the cooling tower to base injcction；Cold wind is roused by centrifugal blower from the cooling tower bottom to top or natural wind forms malleation wind, the liquid thermal material is cooled into into solid granulates；The accumulation solid granulates are stopped by fluid bed；The solid granulates are overflowed by discharging opening；The solid granulates material obtained by said system and method, granule are little, and dissolving is fast, and solution temperature is low, and cooling is thorough, it is easy to high-volume production, and can be prevented effectively from caking phenomenon.
Description
Technical field
This utility model is related to granulating technique field, more particularly to a kind of high tower grit blast crystal system.
Background technology
At present, on the market soft dose of solid-state has lamellar or graininess, in the production process of soft dose of solid-state, generally using flat
Facial steel band cooling conveying pelletize, the dissolving of soft dose of the solid-state obtained by this kind of mode are slow, and solution temperature is high, yields poorly, and
Easily adhesion caking, is unfavorable for preserving and follow-up use, and productivity effect is low.
Utility model content
Main purpose of the present utility model is to propose a kind of high tower grit blast crystal system, it is intended to produce that granule is little, and dissolving is fast,
The low solid granulates material of solution temperature.
For achieving the above object, the utility model proposes high tower grit blast crystal system, which includes cooling tower, for providing
Liquid thermal material crystallisation by cooling is formed into the space of solid granulates；
Injection apparatus, at the top of the cooling tower, for the liquid thermal material in conveyance conduit is drawn to cooling tower,
And by the liquid thermal material with liquid columnar shape from the top of the cooling tower to base injcction；
Centrifugal blower, forms malleation wind for cold wind or natural wind are roused from the cooling tower bottom to top, will be described
Liquid thermal material is cooled into solid granulates；
Fluid bed, positioned at the cooling tower bottom, for stopping the accumulation solid granulates；
Discharging opening, above the fluid bed, for overflowing the solid granulates.
Preferably, the high tower grit blast crystal system also includes pressure release room, connects with the top of cooling tower；
Air-introduced machine, in the pressure release room, for the hot-air in cooling tower is suctioned out to pressure release room, forms negative pressure
Wind；
Control device, for adjusting the wind speed of malleation wind, negative pressure wind, the regulation solid granulates are at the fluid bed
The time of staying.
Preferably, the high tower grit blast crystal system also includes dust arrester, in the pressure release room, for pressure release
Hot-air in room carries out dust removal process；
Odor removal, is connected with the gas discharge outlet in the pressure release room, is removed for carrying out spray to the hot-air after dedusting
Smelly process.
Preferably, the high tower grit blast crystal system also includes vibrosieve, is overflowed by the discharging opening for vibration screening
Solid material.
Preferably, the altitude range of the cooling tower tower body is 15 meters to 25 meters.
Technical solutions of the utility model by liquid thermal material is sprayed from top to bottom in fluid column shape, with centrifugal blower
During the meeting of the cold wind advertised upwards or natural wind, divide rapidly and shrink, in the presence of surface tension, formed tiny
Solid granulates, and continue with action of gravity decline, now, the active force upwards produced due to cold wind or natural wind, then
Make solid granulates accumulate at fluid bed to stop.When certain amount is reached, discharging opening automatically from above fluid bed is overflowed,
Obtain finished product.The solid granulates material obtained by above-mentioned high tower grit blast crystal system, granule are little, and dissolving is fast, and solution temperature is low,
Cooling is thorough, it is easy to high-volume production, and can be prevented effectively from caking phenomenon.
Description of the drawings
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or accompanying drawing to be used is briefly described needed for description of the prior art, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise for not paying creative work
Under, other accompanying drawings can be obtained with the structure according to these accompanying drawings.
Fig. 1 is the structural representation that this utility model high tower grit blast system of crystallization unifies embodiment；
Schematic flow sheets of the Fig. 2 for one embodiment of this utility model high tower grit blast method for crystallising；
Fig. 3 is the concrete refinement schematic diagram of step S300 in Fig. 2；
Schematic flow sheets of the Fig. 4 for another embodiment of this utility model high tower grit blast method for crystallising.
The realization of this utility model purpose, functional characteristics and advantage will be described further in conjunction with the embodiments referring to the drawings.
Specific embodiment
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the present utility model, rather than all
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not making creative work premise
Lower obtained every other embodiment, belongs to the scope of this utility model protection.
It is to be appreciated that the directional instruction (such as up, down, left, right, before and after ...) of institute in this utility model embodiment
It is only used for explaining in the relative position relation under a certain particular pose (as shown in drawings) between each part, motion conditions etc., such as
When really the particular pose changes, then directionality indicates also correspondingly to change therewith.
In addition, the technical scheme between each embodiment of the present utility model can be combined with each other, but must be with this
Field those of ordinary skill can be implemented as basis, should recognize when the combination appearance of technical scheme is conflicting or cannot realize
Combination for this technical scheme is not present, also not within the protection domain that this utility model is required.
The utility model proposes a kind of high tower grit blast crystal system.
Referring to figs. 1 to Fig. 4, Fig. 1 is the structural representation that this utility model high tower grit blast system of crystallization unifies embodiment；Fig. 2
For the schematic flow sheet of one embodiment of this utility model high tower grit blast method for crystallising；Fig. 3 is the concrete refinement of step S300 in Fig. 2
Schematic diagram；Schematic flow sheets of the Fig. 4 for another embodiment of this utility model high tower grit blast method for crystallising.
In this utility model embodiment, as described in Figure 1, the high tower grit blast crystal system includes cooling tower 10, for carrying
Space for liquid thermal material crystallisation by cooling to be formed solid granulates；
Injection apparatus, it is at the top of the cooling tower 10, cold for the liquid thermal material in conveyance conduit 90 is drawn to
But tower 10, and by the liquid thermal material with liquid columnar shape from the top of the cooling tower 10 to base injcction；
Centrifugal blower 30, forms malleation wind for cold wind or natural wind are roused from 10 bottom of the cooling tower to top, will
The liquid thermal material is cooled into solid granulates；
Fluid bed 40, positioned at 10 bottom of the cooling tower, for stopping the accumulation solid granulates；
Discharging opening 50, above the fluid bed 40, for overflowing the solid granulates.
Specifically, the cooling tower 10 of technical solutions of the utility model adopts vertical type cooling tower 10, for for liquid thermal material
Crystallisation by cooling provides reaction compartment into solid granulates, and the altitude range of the cooling tower 10 is preferably 15 meters to 25 meters, concrete numerical value
Here is not limited.Also, liquid is changed into the crystallisation by cooling process of solid matter, belongs to exothermic reaction.In this enforcement
In example, will have substantial amounts of liquid thermal material to be inhaled in tower carries out crystallisation by cooling, will release substantial amounts of heat；In order to reduce extraneous temperature
Impact of the degree to the crystallisation by cooling in cooling tower 10, can also be in the periphery parcel insulation material of the tower body of cooling tower 10.
Injection apparatus include the high-pressure pump 21 being interconnected and shower nozzle 20, generally, the liquid thermal material in conveyance conduit 90
Need to be delivered at the top of cooling tower 10, now from 10 bottom of cooling tower, then can be by liquid thermal material from cooling tower by high-pressure pump 21
10 bottoms are pressed into 10 inner top of cooling tower, and export to shower nozzle 20, and the shower nozzle 20 is loose structure, so as to spray from the shower nozzle 20
The liquid thermal material for going out will be pushed up to bottom of towe from cooling tower 10 with fluid column form and be sprayed.
Summer temp is higher, and the centrifugal blower 30 can be connected with external quenching system 60, and the quenching system 60 is used to produce
Condensing agent of the frozen water of raw refrigeration as Or In Refrigerator, Jing after heat exchange reaction, by Or In Refrigerator blowing cold air, then Jing centrifugal blowers 30
Send in cooling tower 10；And in the winter time or northern cool region, then after can be combined natural wind with quenching system 60, then lead to
Cross centrifugal blower 30 to send in cooling tower 10.The waste of the energy by adopting aforesaid way, can be greatly reduced.
The cold wind or natural wind blasted from centrifugal blower 30 is advertised from 10 bottom of cooling tower to 10 top-direction of cooling tower, with
The liquid thermal material for landing from top to bottom meets in cooling tower 10.As liquid thermal material is sprayed from top to bottom in fluid column shape,
During with the meeting of cold wind or natural wind, divide rapidly and shrink, in the presence of surface tension, form tiny solid-state
Granule, and continue with action of gravity decline, now, produce as centrifugal blower 30 advertises cold wind or natural wind upwards to
On active force, then stop solid granulates accumulation at the fluid bed 40.When certain amount is reached, will automatically from fluid bed 40
The discharging opening 50 of top overflows, and obtains finished product.
The solid granulates material obtained by above-mentioned high tower grit blast crystal system, granule are little, and dissolving is fast, and solution temperature is low,
Cooling is thorough, it is easy to high-volume production, and can be prevented effectively from caking phenomenon.
Specifically, the high tower grit blast crystal system also includes pressure release room 70, connects with the top of cooling tower 10；
Air-introduced machine 71, in the pressure release room 70, for the hot-air in cooling tower 10 is suctioned out to pressure release room 70, shape
Into negative pressure wind；
Control device, for adjusting the wind speed of malleation wind, negative pressure wind, the regulation solid granulates are at the fluid bed 40
The time of staying.
In the present embodiment, centrifugal blower 30 can control its wind speed with air-introduced machine 71 using converter, by adjusting
Section malleation wind, the wind speed of negative pressure wind, so as to adjust solid granulates residence time at the fluid bed 40, control then to discharge when
Between and speed, to ensure being of moderate size for solid granulates.
Also, by the air-introduced machine 71, rapidly the heat in cooling tower 10 can be taken away, so that the temperature in cooling tower 10
It is maintained in constant scope, more stably to carry out crystallisation by cooling reaction.
Specifically, the high tower grit blast crystal system also includes dust arrester 72, in the pressure release room 70, for right
Hot-air in pressure release room 70 carries out dust removal process；
Odor removal 73, is connected with the gas discharge outlet in the pressure release room 70, for spraying to the hot-air after dedusting
Drench deodorizing process.
When extracted out by hot-air, while can also carry substantial amounts of dust into pressure release room 70；Pressure release room
There is in 70 dust arrester 72, the space that the dust arrester 72 can be surrounded by drainage screen is constituted, by the structure of the filter screen type,
Dust is unloaded, other tail gas then enter the space that drainage screen is surrounded, and now, tail gas are sprayed by odor removal 73
After process, then can be emitted in air.By above-mentioned dust arrester 72 and odor removal 73, effective filtered out harmful substance and
Gas, is conducive to environmental conservation.
Generally, the pressure release room 70 adopts 70m3More than space be capable of achieving above-mentioned to filter process.
Specifically, high tower grit blast crystal system also includes vibrosieve 80, selects for vibrosieve 80 and is overflow by the discharging opening 50
The solid material for going out.
Vibrosieve 80 is communicated with also at discharging opening 50, by the specification of 80 mesh screen pore size of vibrosieve, you can screening
Go out to meet the solid granulates of given size.
Additionally, being based on above-mentioned high tower grit blast crystal system, this utility model also provides a kind of high tower grit blast method for crystallising, such as
Described in Fig. 2, which comprises the following steps：
Liquid thermal material in conveyance conduit 90 is drawn to cooling tower by step S100, and by the liquid thermal material with
Liquid columnar shape is from the top of the cooling tower to base injcction；
Step S200, rouses cold wind or natural wind to top from the cooling tower bottom, the liquid thermal material is cooled down shape
Into solid granulates；
The solid granulates are stopped accumulation at the fluid bed of the cooling tower bottom by step S300；
Step S400, overflows the solid granulates from the discharging opening above the fluid bed.
Specifically, above-mentioned cooling tower 10 adopts vertical type cooling tower, for being liquid thermal material crystallisation by cooling into solid granulates
Reaction compartment is provided, the altitude range of the cooling tower 10 is preferably 15 meters to 25 meters, and concrete numerical value here is not limited.Also,
Liquid is changed into the crystallisation by cooling process of solid matter, belongs to exothermic reaction.In the present embodiment, there will be substantial amounts of liquid
Thermal material is inhaled in tower carries out crystallisation by cooling, will release substantial amounts of heat；In order to reduce ambient temperature to cold in cooling tower 10
But the impact for crystallizing, can also be in the periphery parcel insulation material of the tower body of cooling tower 10.
In step S100, generally realized using injection apparatus, injection apparatus include the high-pressure pump 21 being interconnected and shower nozzle
20, generally, the liquid thermal material in conveyance conduit 90 need to be delivered at the top of cooling tower 10, now from 10 bottom of cooling tower, passed through
Liquid thermal material then can be pressed into 10 inner top of cooling tower from 10 bottom of cooling tower by high-pressure pump 21, and export to shower nozzle 20, the spray
20 is loose structure, so as to the liquid thermal material sprayed from the shower nozzle 20 will be pushed up to bottom of towe from cooling tower 10 with fluid column form
Injection.
In step S200, be capable of achieving using centrifugal blower 30, summer temp is higher, the centrifugal blower 30 can with it is outer
Connect quenching system 60 to connect, the quenching system 60 is used for condensing agent of the frozen water as Or In Refrigerator for producing refrigeration, Jing heat exchange reactions
Afterwards, by Or In Refrigerator blowing cold air, then Jing centrifugal blowers 30 are sent in cooling tower 10；And in the winter time or the north coldlyer
Area, then after can be combined natural wind with quenching system 60, then sent in cooling tower 10 by centrifugal blower 30.By using upper
Mode is stated, the waste of the energy can be greatly reduced.
The cold wind or natural wind blasted from centrifugal blower 30 is advertised from 10 bottom of cooling tower to 10 top-direction of cooling tower, with
The liquid thermal material for landing from top to bottom meets in cooling tower 10.As liquid thermal material is sprayed from top to bottom in fluid column shape,
During with the meeting of cold wind or natural wind, divide rapidly and shrink, in the presence of surface tension, form tiny solid-state
Granule, and continue with action of gravity decline, now, produce as centrifugal blower 30 advertises cold wind or natural wind upwards to
On active force, then stop solid granulates accumulation at the fluid bed 40.When certain amount is reached, will automatically from fluid bed 40
The discharging opening 50 of top overflows, and obtains finished product.
The solid granulates material obtained by above-mentioned high tower grit blast method for crystallising, granule are little, and dissolving is fast, and solution temperature is low,
Cooling is thorough, it is easy to high-volume production, and can be prevented effectively from caking phenomenon.
Preferably, as described in Figure 3, step S300 is specifically included：
Step S301, by the hot-air in cooling tower suction out to the pressure release room connected at the top of cooling tower, formed negative pressure wind；
Step S302, adjusts malleation wind, the wind speed of negative pressure wind, adjusts stop of the solid granulates at the fluid bed
Time.
In the present embodiment, step S301 is capable of achieving using air-introduced machine 71, centrifugal blower 30 and air-introduced machine 71
Its wind speed is controlled using converter, by the wind speed for adjusting malleation wind, negative pressure wind, so that solid granulates are adjusted in fluid bed 40
Place's residence time, controls time and the speed for discharging, then to ensure being of moderate size for solid granulates.
Also, by the air-introduced machine 71, rapidly the heat in cooling tower 10 can be taken away, so that the temperature in cooling tower 10
It is maintained in constant scope, more stably to carry out crystallisation by cooling reaction.
Preferably, as described in Figure 3, also include after step S301：
Step S303, carries out dust removal process to the hot-air in pressure release room；
Step S304, is expelled to air after carrying out spray deodorizing process to the hot-air after dedusting.
When extracted out by hot-air, while can also carry substantial amounts of dust into pressure release room 70；Pressure release room
There is in 70 dust arrester 72, the space that the dust arrester 72 can be surrounded by drainage screen is constituted, by the structure of the filter screen type,
Dust is unloaded, other tail gas then enter the space that drainage screen is surrounded, and now, tail gas are sprayed by odor removal 73
After process, then can be emitted in air.By above-mentioned dust arrester 72 and odor removal 73, effective filtered out harmful substance and
Gas, is conducive to environmental conservation.
Generally, the pressure release room 70 adopts 70m3More than space be capable of achieving above-mentioned to filter process.
Preferably, as described in Figure 4, also include after step S400：
Step S500, the solid material to being overflowed by the discharging opening carry out vibration screening.
Vibrosieve 80 is communicated with also at discharging opening 50, by the specification of 80 mesh screen pore size of vibrosieve, you can screening
Go out to meet the solid granulates of given size.
Preferred embodiment of the present utility model is the foregoing is only, the scope of the claims of the present utility model is not thereby limited,
It is every utility model of the present utility model design under, the equivalent structure made using this utility model description and accompanying drawing content
Conversion, or directly/be used in indirectly other related technical fields and be included in scope of patent protection of the present utility model.
Claims (5)
1. a kind of high tower grit blast crystal system, it is characterised in that include：
Cooling tower, for providing the space that liquid thermal material crystallisation by cooling is formed solid granulates；
Injection apparatus, at the top of the cooling tower, for the liquid thermal material in conveyance conduit is drawn to cooling tower, and will
The liquid thermal material with liquid columnar shape from the top of the cooling tower to base injcction；
Centrifugal blower, forms malleation wind for cold wind or natural wind are roused from the cooling tower bottom to top, by the liquid
Thermal material is cooled into solid granulates；
Fluid bed, positioned at the cooling tower bottom, for stopping the accumulation solid granulates；
Discharging opening, above the fluid bed, for overflowing the solid granulates.
2. high tower grit blast crystal system as claimed in claim 1, it is characterised in that also include
Pressure release room, connects with the top of cooling tower；
Air-introduced machine, in the pressure release room, for the hot-air in cooling tower is suctioned out to pressure release room, forms negative pressure wind；
Control device, for adjusting the wind speed of malleation wind, negative pressure wind, adjusts stop of the solid granulates at the fluid bed
Time.
3. high tower grit blast crystal system as claimed in claim 2, it is characterised in that also include
Dust arrester, in the pressure release room, for carrying out dust removal process to the hot-air in pressure release room；
Odor removal, is connected with the gas discharge outlet in the pressure release room, for carrying out spraying at deodorization to the hot-air after dedusting
Reason.
4. high tower grit blast crystal system as claimed in claim 1, it is characterised in that also include
Vibrosieve, for the solid material that vibration screening is overflowed by the discharging opening.
5. the high tower grit blast crystal system as any one of Claims 1-4, it is characterised in that the cooling tower tower body
Altitude range be 15 meters to 25 meters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620840009.8U CN206045962U (en) | 2016-08-03 | 2016-08-03 | High tower grit blast crystal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620840009.8U CN206045962U (en) | 2016-08-03 | 2016-08-03 | High tower grit blast crystal system |
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| Publication Number | Publication Date |
|---|---|
| CN206045962U true CN206045962U (en) | 2017-03-29 |
Family
ID=58379962
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620840009.8U Expired - Fee Related CN206045962U (en) | 2016-08-03 | 2016-08-03 | High tower grit blast crystal system |
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| CN (1) | CN206045962U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111644122A (en) * | 2020-04-29 | 2020-09-11 | 天津科技大学 | Hot-melting spouted bed granulation device and method |
-
2016
- 2016-08-03 CN CN201620840009.8U patent/CN206045962U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111644122A (en) * | 2020-04-29 | 2020-09-11 | 天津科技大学 | Hot-melting spouted bed granulation device and method |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170329 Termination date: 20200803 |