CN100342191C - Device for continuously fast preparing ice paste or hydrate paste and application thereof - Google Patents
Device for continuously fast preparing ice paste or hydrate paste and application thereof Download PDFInfo
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- CN100342191C CN100342191C CNB2005101008158A CN200510100815A CN100342191C CN 100342191 C CN100342191 C CN 100342191C CN B2005101008158 A CNB2005101008158 A CN B2005101008158A CN 200510100815 A CN200510100815 A CN 200510100815A CN 100342191 C CN100342191 C CN 100342191C
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- 238000004781 supercooling Methods 0.000 claims abstract description 99
- 239000002002 slurry Substances 0.000 claims abstract description 83
- 230000007306 turnover Effects 0.000 claims description 3
- 238000009826 distribution Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 15
- 230000008569 process Effects 0.000 abstract description 10
- 238000002360 preparation method Methods 0.000 abstract description 6
- 230000003068 static effect Effects 0.000 abstract description 6
- 239000013078 crystal Substances 0.000 abstract description 3
- 230000035939 shock Effects 0.000 abstract description 2
- 239000007790 solid phase Substances 0.000 abstract description 2
- 239000007791 liquid phase Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- 238000004378 air conditioning Methods 0.000 description 14
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 13
- 239000007788 liquid Substances 0.000 description 12
- 229910001220 stainless steel Inorganic materials 0.000 description 10
- 239000010935 stainless steel Substances 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 7
- 238000003860 storage Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000005057 refrigeration Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000012071 phase Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 239000013526 supercooled liquid Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 230000008447 perception Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
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- 238000000926 separation method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005496 eutectics Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000006193 liquid solution Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 201000009240 nasopharyngitis Diseases 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- RKHXQBLJXBGEKF-UHFFFAOYSA-M tetrabutylphosphanium;bromide Chemical compound [Br-].CCCC[P+](CCCC)(CCCC)CCCC RKHXQBLJXBGEKF-UHFFFAOYSA-M 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
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- Other Air-Conditioning Systems (AREA)
Abstract
The present invention provides a high efficiency device for continuously fast preparing mixed ice slurry or hydrate slurry of solid phase and liquid phase and application of the device in the preparation of the ice slurry or hydrate slurry. The device of the present invention comprises a heater 3, a supercooling heat exchanger 1, an ultrasonic supercooling removing device 2 and a conveying pump 4, which are orderly connected end to end, wherein the ultrasonic supercooling removing device 2 comprises a casing 22 and an ultrasonic oscillator box 210 encapsulated in the casing 22, the casing 22 and the ultrasonic oscillator box 210 form an inner cavity 212 which is respectively communicated with an inlet pipe 23 and an outlet pipe 21, the inlet pipe 23 is connected with the supercooling heat exchange 1, and the outlet pipe 21 is connected with the conveying pump 4. The device of the present invention can be applied to the preparation of the ice slurry or the hydrate slurry. The whole device system can realize the continuously fast preparing process of the ice slurry (the hydrate slurry) with high efficiency, compared with the methods, such as mechanical shock crystal promotion, etc., in traditional static ice preparation and dynamic ice preparation, the speed and the efficiency of the ice preparation are greatly improved.
Description
Technical field
The present invention relates to a kind of continuously quick manufacturing installation system that is applicable to ice slurry or hydrate slurry, the present invention also relates to the application of this device in preparation ice slurry and hydrate slurry simultaneously.
Background technology
In more prevalent cold accumulation air-conditioner and emerging high density latent heat central air-conditioning, cold stores or the mode of carrying has been become by traditional temperature difference sensible heat that utilizes single-phase medium and utilizes medium generation liquid---the latent heat when solid phase becomes.The former is as water cold accumulation air-conditioner, common cold water formula central air-conditioning etc., the latter such as various ice-storage air-conditioning, hydrate cold accumulation air-conditioner and by solid---and the ice slurry of liquid two-phase coexistent or hydrate slurry are as carrying the high density latent heat central air-conditioning etc. that the refrigerant body is delivered directly to air conditioning terminal.These are undertaken by latent heat of phase change that cold stores or the high density of carrying is carried the refrigerant body and mainly comprised ice and various eutectic salts hydrate (warm ice).Therefore, ice or hydrate crystal has manufactured key problem in ice-storage air-conditioning or the hydrate latent heat air-conditioning technical.
Ice-storage air-conditioning can be divided into static cold-storage and the dynamic ice cold-storage dual mode iced, and the manufacturing of corresponding ice (hydrate) also can be divided into static and dynamic dual mode.Static ice making is meant in fixing cold-storage groove or container water is cooled to statically till forming ice cube, as various ice coiled pipe types, ice ball type etc.Dynamic ice-making is meant that then the generation of ice and storing process carry out in dynamic circulation, as ice making landing formula etc.Though the simple operation easily of the method for static ice making, because the thermal resistance of ice is bigger, the heat transfer conditions during ice making is abominable, and the formation speed of ice is slow, and needs bigger degree of supercooling, and this makes that the Energy Efficiency Ratio (COP) of refrigeration machine is low.Dynamic ice-making then can increase substantially ice making efficient.Because the generation of ice is finished in dynamic flow process, do not exist ice cube to pile up and hinder the problem of conducting heat.On the other hand, the degree of supercooling during ice making does not need very big, can allow the COP of refrigeration machine make moderate progress like this.Therefore, the method for dynamic ice-making has fairly obvious technical advantage, is becoming the main flow trend of ice-making technology in ice cold-storage and the hydrate air-conditioning gradually.
At present, state-of-the-art dynamic ice-making process is to adopt first supercooling to remove overcooled method manufacturing ice slurry again.Idiographic flow is exactly, in subcooler water (perhaps hydrated salt solution) supercooling to certain degree, deliver to then in the supercooling decontrol and remove supercooled state, generate the mixed ice slurry (perhaps hydrate slurry) of solid-liquid.The ice slurry that generates can be sent to the frozen water separator or directly be sent to air conditioning terminal.Because the mixed ice slurry of solid-liquid has good flowability, ice-making process can be realized real dynamic circulation, and ice making efficient improves greatly.The present invention is based on this dynamic ice-making principle, designed the continuously quick manufacturing installation system of high efficiency suitable ice slurry of a cover or hydrate slurry.
Summary of the invention
The object of the present invention is to provide and a kind ofly can make the mixed ice slurry of solid-liquid two-phase or the apparatus system of hydrate slurry efficiently, continuously, fast.
Another object of the present invention provides the application of apparatus of the present invention in making ice slurry or hydrate slurry.
Above-mentioned purpose of the present invention adopts following technical scheme to realize: a kind of device for continuously fast preparing of icing slurry or hydrate slurry, it comprises preheater, supercooling heat exchanger, ultrasonic wave supercooling decontrol and the delivery pump that head and the tail connect successively
Apparatus system of the present invention comprises three parts, i.e. supercooling heat exchanger, ultrasonic wave supercooling remover and preheater.Above-mentioned three parts constitute three closed circuits with refrigeration machine and auxiliary thermal source, a heat exchanger channels of described supercooling heat exchanger links to each other with the evaporimeter of refrigeration machine and constitutes the low-temperature receiver circulation, and the effect of this circulation is that the cold of evaporator of refrigerator is passed to the supercooling heat exchanger; Another heat exchanger channels of supercooling heat exchanger is connected to become ice slurry (hydrate slurry) with heat exchanger channels of preheater and ultrasonic wave supercooling remover and generates loop continuously fast; Another heat exchanger channels of preheater is communicated with the formation warm-up cycle with auxiliary thermal source.In addition, comprise a delivery pump in the generation loop fast continuously at ice slurry (hydrate slurry), for this loop provides circulation power.
Described supercooling heat exchanger is a plate type heat exchanger.
Connecting leg between described supercooling heat exchanger and the ultrasonic wave supercooling remover is provided with a temperature sensor.
On the outlet connecting leg of described ultrasonic wave supercooling remover delivery pump is housed.
Described preheater is plate type heat exchanger or shell-and-tube heat exchanger or double pipe heat exchanger, and the connecting leg between preheater and the supercooling heat exchanger is provided with a temperature sensor.
Described ultrasonic wave supercooling remover comprises housing and is encapsulated in the ultrasonic oscillator box of described enclosure interior, described housing becomes an inner chamber with described ultrasonic oscillator box-like, this inner chamber connects with inlet tube and outlet respectively, described inlet tube connects the supercooling heat exchanger, and described outlet connects delivery pump.The built-in some ultrasonic oscillators that link to each other with power supply of described ultrasonic oscillator box, the formed ultrasonic wave surface of emission of described ultrasonic oscillator is over against the central shaft of described inner chamber.The inner chamber of described ultrasonic wave supercooling remover is exactly the place that supercooling is removed.Housing is respectively equipped with inlet tube and outlet in two ends up and down, and the center, top is provided with blast pipe.
Described ultrasonic oscillator box is made up of ultrasonic oscillator, stainless steel casing and ultrasonic oscillator power supply lead wire.The equally spaced cuboid stainless steel casing inside that is arranged in the square-section of some ultrasonic oscillators, the surface of emission of all ultrasonic oscillators all is attached on the same inner surface of stainless steel casing, the pairing outer surface of this inner surface is exactly the surface of emission of ultrasonic oscillator box, it removes the central shaft of place inner chamber over against above-mentioned supercooling in the supercooling remover, so that launch uniform ultrasonic wave in cylindrical cavity.The place is the opening except that the ultrasonic oscillator power supply lead wire, and the ultrasonic oscillator box is all sealings, and its inside and outside is isolated, invades the corrosion ultrasonic oscillator to prevent liquid.
The power supply lead wire place of described ultrasonic oscillator box is provided with power supply lead wire stainless steel sleeve pipe, and the sleeve outer wall face is processed with screw thread.The oscillator box overall package is in described housing, and power supply stainless steel sleeve pipe is wrapped in the oscillator power supply lead wire and stretches out from the housing round hole, and makes housings close by rubber washer and clamp nut.On the other hand, stainless steel power supply lead wire sleeve pipe and clamp nut also play the fixedly effect of oscillator box.
In the square cavity of described shell inner surface, arrange two identical above-mentioned ultrasonic oscillator boxes.The ultrasonic oscillator box is vertically placed, and the ultrasonic oscillator box surface of emission is arranged on the circumference in enclosure interior cylindrical cavity cross section, with the cylindrical shape of the maintenance inner chamber of maximum possible.Two ultrasonic oscillator boxes are 120 degree at upper edge, horizontal cross-section enclosure interior inner chamber circumference and distribute, the purpose of Bu Zhiing is in order to make two ultrasonic oscillator box ultrasonic waves transmitted mutual oblique in the housing inner chamber like this, to make in inner chamber not only strongly but also ultrasound field cavitation disturbance uniformly.
On the upper side of described housing, be furnished with an inlet tube, be furnished with an outlet on the lower side.Import and export Guan Jun and draw, and the direction of rotation of current turnover is identical along the tangent to periphery direction level of enclosure interior inner chamber.Such import and export pipe arrangement is in order to make current rotate disturbance after entering the enclosure interior inner chamber, so that current are accepted ultrasonic wave radiation more uniformly in inner chamber.
Described case top has a blast pipe, and blast pipe is equipped with stop valve.Can get rid of foreign gas in the housing by stop valve, also can be used as the high-pressure security protection measure.
Apparatus of the present invention can be applicable to make ice slurry or hydrate slurry.Aqueous water or hydrate soln at first are admitted to preheating in the preheater 3, enter then in the supercooling heat exchanger 1 by supercooling, after coming out, cooled liquid directly enters ultrasonic wave supercooling remover 2 from supercooling heat exchanger 1, in ultrasonic wave supercooling remover 2, generate ice slurry or hydrate slurry rapidly through action of ultrasonic waves, be transported in the frozen water separator by delivery pump 4 at last and implement Separation of Solid and Liquid, aqueous water or hydrate soln are sent to preheater 3 again, finish a circulation.Apparatus of the present invention system has realized the efficient quick and continuous circulation manufacture process of ice slurry or hydrate slurry thus.
The effect of preheater 3 is to prevent that the aqueous water or the hydrate soln that enter supercooling heat exchanger 1 from freezing in supercooling heat exchanger 1 in advance because containing tiny ice pellets, thus the danger that supercooling heat exchanger 1 takes place to stop up.Preheater 3 judges whether to open warm-up operation according to the temperature sensor 5 of supercooling heat exchanger 1 porch.The auxiliary thermal source of preheater 3 can be special electrical heating, also can be the recovery heat of air-conditioning condenser or cooling tower, can select for use according to actual conditions.
It is identical with making the ice slurry that apparatus of the present invention are applied to make the basic principle and the flow process of hydrate slurry, just controls different the getting final product of temperature at each control point according to the character of different material.
Apparatus of the present invention system adopts plate type heat exchanger as the supercooling heat exchanger, and heat exchange efficiency is very high; Adopt ultrasonic wave supercooling remover to impel supercooled liquid to generate ice slurry (hydrate slurry), short brilliant efficient significantly improves, and ice slurry (hydrate slurry) formation speed increases considerably; Adopt preheater can prevent effectively that thereby liquid from solidifying blocking heat-exchanger too early in the supercooling heat exchanger.Whole apparatus system can be realized efficiently, ice slurry (hydrate slurry) manufacture process continuously, fast, and compared with methods such as traditional static ice making and the short crystalline substances of the mechanical shock in the dynamic ice-making, the speed and the efficient of ice making all are improved significantly.
Description of drawings
Fig. 1 is that the system of apparatus of the present invention forms schematic diagram;
Fig. 2 is the structural representation of embodiment of the invention ultrasonic wave supercooling decontrol;
Fig. 3 is the cutaway view of Fig. 2.
Description of reference numerals
1 supercooling heat exchanger
2 ultrasonic wave supercooling decontrols
3 preheaters
4 delivery pumps
5 temperature sensors
6 temperature sensors
21 outlets
22 housings
23 inlet tubes
24 stop valves
25 blast pipes
26 ultrasonic oscillator power supply lead wires
27 power supply lead wire stainless steel sleeve pipes
28 nuts
29 seal gaskets
210 ultrasonic oscillator boxes
211 surface of emissions
212 inner chambers
The specific embodiment
As shown in Figure 1, a kind of device for continuously fast preparing of icing slurry or hydrate slurry of the present invention, it comprises preheater 3, supercooling heat exchanger 1, ultrasonic wave supercooling decontrol 2 and the delivery pump 4 that head and the tail connect successively, between preheater 3 and the supercooling heat exchanger 1 temperature sensor 5 is housed, between supercooling heat exchanger 1 and the ultrasonic wave supercooling decontrol 2 temperature sensor 6 is housed also.
Supercooling heat exchanger 1 is a plate type heat exchanger, and preheater 3 is plate type heat exchanger or shell-and-tube heat exchanger or double pipe heat exchanger.
As Fig. 2, shown in Figure 3, ultrasonic wave supercooling decontrol 2 among the present invention comprises housing 22 and is encapsulated in two ultrasonic oscillator boxes 210 of housing 22 inside, housing 22 and ultrasonic oscillator box 210 form 212, two ultrasonic oscillator boxes 210 of a cylindrical cavity and are 120 degree distributions at upper edge, horizontal cross-section inner chamber 212 circumference.Inner chamber 212 connects with inlet tube 23 that is arranged in housing 22 upper side and the outlet 21 that is arranged in housing 22 lower side respectively, inlet tube 23 connects supercooling heat exchanger 1, outlet 21 connects pump 4, inlet tube 23 and outlet 21 are all drawn along the tangent to periphery direction level of housing inner chamber 212, and the direction of rotation of current turnover is identical.Place some ultrasonic oscillators that link to each other with power supply by ultrasonic oscillator power supply lead wire 26 in the ultrasonic oscillator box 210 equally spacedly, the formed ultrasonic wave surface of emission 211 of ultrasonic oscillator is over against the central shaft of inner chamber 212.Have a blast pipe 25 at housing 22 tops, blast pipe 25 is equipped with stop valve 24.
Ultrasonic oscillator power supply lead wire 26 places of ultrasonic oscillator box 210 are provided with power supply lead wire stainless steel sleeve pipe 27, power supply lead wire stainless steel sleeve pipe 27 is wrapped in ultrasonic oscillator power supply lead wire 26 and stretches out from housing 22 round holes, and makes housing 22 sealings by rubber seal rubber cushion 29 and clamp nut 28.On the other hand, power supply lead wire stainless steel sleeve pipe 27 and clamp nut 28 also play the effect of mounting ultrasonic oscillator box 210.
Three devices of apparatus of the present invention system, be that supercooling heat exchanger 1, ultrasonic wave supercooling remover 2 and preheater 3 constitute three closed circuits (as shown in Figure 1) with refrigeration machine and auxiliary thermal source, a heat exchanger channels of described supercooling heat exchanger 1 links to each other with the evaporimeter of refrigeration machine and constitutes the low-temperature receiver circulation, and the effect of this circulation is that the cold of evaporator of refrigerator is passed to supercooling heat exchanger 1; Another heat exchanger channels of supercooling heat exchanger 1 is connected to become ice slurry (hydrate slurry) with heat exchanger channels of preheater 3 and ultrasonic wave supercooling decontrol 2 and generates loop continuously fast; Another heat exchanger channels of preheater 3 is communicated with the formation warm-up cycle with auxiliary thermal source.In addition, comprise a delivery pump 4 in the generation loop fast continuously at ice slurry (hydrate slurry), for this loop provides circulation power.
Must vertically place when wherein ultrasonic wave supercooling decontrol 2 uses.As shown in Figure 2.The supercooling liquid that comes out from supercooling heat exchanger 1 enters ultrasonic wave supercooling decontrol 2 by inlet tube 3.Because inlet tube 23 is with the direction gatherer inner cylindrical inner chamber 212 of horizontal tangent, as shown in Figure 3, supercooling liquid rotates once entering ultrasonic wave supercooling decontrol 2 inner generations.Because the outlet 21 of ultrasonic wave supercooling decontrol 2 is also derived ultrasonic wave supercooling decontrol inner cylinder inner chamber 212 with the tangential direction of identical direction of rotation, will cross device with the mode rotating flow under the screw at 212 li fluids of interior cylindrical inner chamber of whole device so again.The surface of emission 211 of two ultrasonic oscillator boxes 210 that is 120 degree pitch arrangement along circumference is over against the central shaft of inner cylinder inner chamber 212, and the supercooled liquid radiation to the inner chamber 212 of flowing through in a spiral manner in is two ultrasonic array that 120 degree interlock.After supercooled liquid experienced the ultrasonic wave radiation of enough time from top to bottom, tiny crystal ice granule began to form, and had generated ice (hydrate) slurry of enough concentration when arriving bottom of device, was discharged by outlet 21 at last.
Apparatus of the present invention can be applicable to make the ice slurry.The aqueous water that comes out from the frozen water separator at first is admitted to and is preheating to 0.5 ℃ in the preheater 3, enter then in the supercooling heat exchanger 1 by supercooling to-2 ℃ (being that degree of supercooling is 2 ℃), after coming out, subcooled water under-2 ℃ directly enters ultrasonic wave supercooling remover 2 from supercooling heat exchanger 1, in ultrasonic wave supercooling remover 2, generate the ice slurry rapidly through action of ultrasonic waves, be transported to by pump 4 at last and implement the frozen water separation in the frozen water separator, solid ice is stored, aqueous water is sent to preheater 3 again, finishes a circulation.Apparatus of the present invention system has realized the efficient quick and continuous circulation manufacture process of ice slurry thus.
The effect of preheater 3 is to prevent that the aqueous water that enters supercooling heat exchanger 1 from freezing in supercooling heat exchanger 1 in advance because containing tiny ice pellets, thus the danger that supercooling heat exchanger 1 takes place to stop up.Preheater 3 judges whether to open warm-up operation according to the temperature sensor 5 of supercooling heat exchanger 1 porch, if the temperature of the inlet aqueous water of the supercooling heat exchanger 1 of sensor 5 perception is lower than 0.5 ℃, then send the instruction of opening warm-up operation, otherwise do not carry out warm-up operation.The auxiliary thermal source of preheater 3 can be special electrical heating, also can be the recovery heat of air-conditioning condenser or cooling tower, can select for use according to actual conditions.
Apparatus of the present invention also can be applicable to make hydrate slurry, and basic principle and flow process are identical with making the ice slurry, just the temperature difference at each control point.Be that 22% ratio makes the refrigerating medium of tetrabutyl phosphonium bromide aqueous ammonium as present embodiment with mass concentration below, its phase transition temperature is 9 ℃.
The liquid solution of returning from air conditioner end equipment or solid-liquid separator at first enters preheater 3 and is preheating to 10 ℃ (this temperature can guarantee no longer to contain in the solution solid-state hydrate particle, thereby can not generating hydrate in advance, the solution that guarantees to enter supercooling heat exchanger 1 do not stop up heat exchanger), certainly, if entering the solution temperature of supercooling heat exchanger 1 inlet, temperature sensor 5 perception are higher than 10 ℃ then do not carry out warm-up operation, 10 ℃ solution enters in the supercooling heat exchanger 1 by supercooling to 7 ℃ (by temperature sensor 6 controls of supercooling heat exchanger 1 outlet) again, 7 ℃ over-cooled solution enters and generates hydrate slurry in the ultrasonic wave supercooling remover 2 fast, be transported to solid-liquid separator or the past air conditioning terminal of direct pump by delivery pump 4 at last, the solution of returning from separator or air conditioning terminal is sent to preheater 3 again, finishes a circulation.
Claims (10)
1, a kind of device for continuously fast preparing of icing slurry or hydrate slurry, it is characterized in that: it comprises preheater (3), supercooling heat exchanger (1), ultrasonic wave supercooling decontrol (2) and the delivery pump (4) that head and the tail connect successively; Described ultrasonic wave supercooling decontrol (2) comprises housing (22) and is encapsulated in the inner ultrasonic oscillator box (210) of described housing (22), described housing (22) and described ultrasonic oscillator box (210) form an inner chamber (212), this inner chamber (212) connects with inlet tube (23) and outlet (21) respectively, described inlet tube (23) connects supercooling heat exchanger (1), and described outlet (21) connects delivery pump (4); The built-in some ultrasonic oscillators that link to each other with power supply of described ultrasonic oscillator box (210), the formed ultrasonic wave surface of emission of described ultrasonic oscillator (211) is over against the central shaft of described inner chamber (212).
2, a kind of device for continuously fast preparing of icing slurry or hydrate slurry according to claim 1, it is characterized in that: between described preheater (3) and the described supercooling heat exchanger (1) temperature sensor is housed, between described supercooling heat exchanger (1) and the described ultrasonic wave supercooling decontrol (2) temperature sensor is housed also.
3, a kind of device for continuously fast preparing of icing slurry or hydrate slurry according to claim 1, it is characterized in that: described supercooling heat exchanger (1) is a plate type heat exchanger.
4, a kind of slurry or device for continuously fast preparing of hydrate slurry iced according to claim 1 is characterized in that: described preheater (3) is for one of following: plate type heat exchanger, shell-and-tube heat exchanger, double pipe heat exchanger.
5, a kind of device for continuously fast preparing of icing slurry or hydrate slurry according to claim 1, it is characterized in that: it is cylindrical that described inner chamber (212) is class.
6, a kind of according to claim 1 or 5 device for continuously fast preparing of icing slurry or hydrate slurry, it is characterized in that: described ultrasonic oscillator box (210) is two, and is 120 degree distributions at the described inner chamber in upper edge, horizontal cross-section (212) circumference.
7, a kind of according to claim 1 or 5 device for continuously fast preparing of icing slurry or hydrate slurry, it is characterized in that: described inlet tube (23) is arranged in the upper side of described housing (22), described outlet (21) is arranged in the lower side of described housing (22), both all draw along the tangent to periphery direction level of housing inner chamber (212), and the direction of rotation of current turnover is identical.
8, a kind of according to claim 1 or 5 device for continuously fast preparing of icing slurry or hydrate slurry, it is characterized in that: described housing (22) top has a blast pipe (25), and described blast pipe (25) is equipped with stop valve (24).
9, the application of the device for continuously fast preparing of described ice slurry of a kind of claim 1 or hydrate slurry, wherein said device for continuously fast preparing is applied in to be made in the ice slurry.
10, the application of the device for continuously fast preparing of described ice slurry of a kind of claim 1 or hydrate slurry, wherein said device for continuously fast preparing is applied in to be made in the hydrate slurry.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101008158A CN100342191C (en) | 2005-10-31 | 2005-10-31 | Device for continuously fast preparing ice paste or hydrate paste and application thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101008158A CN100342191C (en) | 2005-10-31 | 2005-10-31 | Device for continuously fast preparing ice paste or hydrate paste and application thereof |
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| Publication Number | Publication Date |
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| CN1786626A CN1786626A (en) | 2006-06-14 |
| CN100342191C true CN100342191C (en) | 2007-10-10 |
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| CNB2005101008158A Expired - Fee Related CN100342191C (en) | 2005-10-31 | 2005-10-31 | Device for continuously fast preparing ice paste or hydrate paste and application thereof |
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Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102052814B (en) * | 2010-12-31 | 2012-06-06 | 东莞理工学院 | Fluidized ice slurry generating system for alternate refrigeration |
| CN102514776B (en) * | 2011-12-21 | 2014-06-04 | 浙江海洋学院普陀科学技术学院 | Packing machine for binary ice water products |
| CN102589219B (en) * | 2012-01-21 | 2014-08-06 | 江卫红 | Ultrasonic subcooling eliminating device |
| CN102589221A (en) * | 2012-03-30 | 2012-07-18 | 苏州市思玛特电力科技有限公司 | Device and method using ultrasonic wave for preparing ice slurry |
| CN102679653B (en) * | 2012-05-16 | 2014-09-03 | 广州鑫誉蓄能科技有限公司 | Supercooling relief device in high-voltage discharge mode |
| CN102679654B (en) * | 2012-05-16 | 2014-07-09 | 广州鑫誉蓄能科技有限公司 | Supercooling disable device utilizing high-pressure water jet mode |
| CN105928273A (en) * | 2016-04-19 | 2016-09-07 | 中南大学 | Device for preventing ice blockage during supercooling process ice slurry production by utilizing residual heat and control method thereof |
| CN111595075A (en) * | 2019-02-20 | 2020-08-28 | 烟台冰轮节能科技有限公司 | Air-cooled direct expansion type supercooled water ice slurry unit |
| CN110345665A (en) * | 2019-06-10 | 2019-10-18 | 湖北风神净化空调设备工程有限公司 | A kind of ice source heat pump system that ice content is controllable |
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| US6647739B1 (en) * | 2002-10-31 | 2003-11-18 | Samsung Gwangju Electronics Co., Ltd. | Ice making machine |
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| CN2417406Y (en) * | 2000-03-01 | 2001-01-31 | 清华同方股份有限公司 | Micro ice crystal eliminating device for overcold water dynamic ice producing system of ice cold storage air conditioner |
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| US6647739B1 (en) * | 2002-10-31 | 2003-11-18 | Samsung Gwangju Electronics Co., Ltd. | Ice making machine |
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| CN1786626A (en) | 2006-06-14 |
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Application publication date: 20060614 Assignee: China Guangdong Nuclear Energy Industry Development Co. Ltd. Assignor: Guangzhou Senyo Thermal Storage Technology Co., Ltd. Contract record no.: 2013440020425 Denomination of invention: Device for continuously fast preparing ice paste or hydrate paste and application thereof Granted publication date: 20071010 License type: Exclusive License Record date: 20131227 |
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Application publication date: 20060614 Assignee: China Guangdong Nuclear Energy Industry Development Co. Ltd. Assignor: Guangzhou Senyo Thermal Storage Technology Co., Ltd. Contract record no.: 2013440020425 Denomination of invention: Device for continuously fast preparing ice paste or hydrate paste and application thereof Granted publication date: 20071010 License type: Exclusive License Record date: 20131227 |
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