CN106461286A - Ultra low temperature freezer - Google Patents
Ultra low temperature freezer Download PDFInfo
- Publication number
- CN106461286A CN106461286A CN201580025533.8A CN201580025533A CN106461286A CN 106461286 A CN106461286 A CN 106461286A CN 201580025533 A CN201580025533 A CN 201580025533A CN 106461286 A CN106461286 A CN 106461286A
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- Prior art keywords
- refrigerant pipe
- volume
- superfreeze
- pipe
- storehouse
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Disclosed is an ultra low temperature freezer in which a double pipe is formed so that the volume of the double pipe for performing heat exchange between a refrigerant discharged from a condenser and a refrigerant discharged from an evaporator is 70% to 130% relative to the volume of an evaporation pipe, thereby rapidly lowering the temperature of the refrigerants to the ultra low temperature as the cooling cycle of the refrigerants is repeated. To this end, the present invention provides an ultra low temperature freezer comprising an evaporator having an evaporation pipe, a compressor, an expansion pipe, and a condenser, the freezer further comprising a first refrigerant pipe which is provided between the condenser and the expansion pipe and which is connected between the condenser and the expansion pipe, and a second refrigerant pipe which receives the first refrigerant pipe therein to form a double pipe and which is connected between the evaporator and the compressor, wherein the volume difference between the volume of the second refrigerant pipe and the volume of the first refrigerant pipe may be 70% to 130% relative to the volume of the evaporation pipe.
Description
Technical field
The present invention relates to a kind of superfreeze storehouse.Specifically it is simply that being related to one kind not separately using such as low temperature
(Cryogenic) cold-producing medium of cold-producing medium etc., just can be made with universal architecture by the volume of adjusting sleeve pipe (double pipe)
Refrigerator IQF to subzero 80 degree of temperature below superfreeze storehouse.
Background technology
Refrigerator has compressor, freezing machine, decompressor and rapid steamer, and the cooling using compression-condensing-expansion-evaporation follows
Ring is cooling down refrigerating chamber.
Cooling circulation includes：Operating the compression of the refrigerant compression of gaseous state to high tcmpcrauire-higb pressure by compressor
Circulation；Condensation cycle by the gas-condensate liquid of boil down to high tcmpcrauire-higb pressure；Reduce the expansion cycles of condensed gas pressure；Will
The cold-producing medium that pressure reduces vaporizes thus reducing the vaporization cycle of freezer temperature.
By in the above-mentioned cooling refrigerator that constitutes of circulation, by connection sleeve pipe between freezing machine and decompressor, using from
Evaporimeter discharge low temperature/low pressure refrigerant come to cool down from freezing machine discharge cold-producing medium, thus improving the refrigerating efficiency of refrigerator.
In this case, sleeve pipe includes：The 1st refrigerant pipe from freezing machine to decompressor；Accommodate the 1st refrigerant pipe and be connected to
The 2nd refrigerant pipe between rapid steamer and compressor.Make the cold-producing medium from freezing machine discharge sufficiently cool using sleeve pipe, Ke Yiti
The refrigeration of the cooling circulation that height is made up of compressor-freezing machine-decompressor-rapid steamer.
As an example of the refrigerator using sleeve pipe, in Ebrean Registered Patent the 10-0836824th, there is related record.
By the use of dry ice (carbon dioxide) as cold-producing medium in registered patent the 10-0836824th, in order to reduce because of electric power storage to greatest extent
The volume that pond is caused increases, and makes the 1st stream being connected with gas cooler outlet side and the 2nd stream being connected with rapid steamer outlet side
Road mutually carries out heat exchange.In this case, registered patent the 10-0836824th makes the 1st stream towards the lower section stream of body
Dynamic, thus without separately installing battery, refrigerator body can be made compacter.But, such as registered patent 10-0836824
Number Fig. 5 shown in, registered patent the 10-0836824th is that sleeve pipe is configured to band wound coil shape, therefore, sleeve pipe itself
Volume can make refrigerator structure realize densification to be restricted in addition it is also necessary to dry ice be used as cold-producing medium.And, it uses sleeve pipe
Purpose seems not lying in raising refrigerating efficiency, and is only that and so that the cold-producing medium in sleeve pipe is flowed downwards thus removing battery,
The technology with regard to IQF that therefore not there are considers.
Content of the invention
Technical problem to be solved
It is an object of the invention to, provide a kind of superfreeze storehouse, by the cold-producing medium discharged from freezing machine with from evaporation
The ratio of sleeve pipe volume and the volume of evaporation tube that the cold-producing medium that machine is discharged carries out heat exchange is set as 70%～130%, thus with
The cooling circulating repetition of cold-producing medium, the temperature of cold-producing medium can promptly be down to the ultralow temperature of setting.
The method solving technical problem
To achieve these goals, may include according to the superfreeze storehouse of the embodiment of the present invention：Accommodate the steaming of evaporation tube
Send out machine, compressor, expansion tube, freezing machine, sleeve pipe.In this case, sleeve pipe includes：Configuration freezing machine and expansion tube it
Between, and it is connected to the 1st refrigerant pipe between freezing machine and expansion tube；Inner containment the 1st refrigerant pipe forms sleeve pipe, and connects
The 2nd refrigerant pipe between rapid steamer and compressor.Compared to the volume of evaporation tube, the volume of the 2nd refrigerant pipe and the 1st system
The difference of the volume of refrigerant tube is difference volume is 70%～130%.
To achieve these goals, may include according to the superfreeze storehouse of the embodiment of the present invention：Accommodate the steaming of evaporation tube
Send out machine, compressor, expansion tube, freezing machine, sleeve pipe.In this case, sleeve pipe includes：Configuration freezing machine and expansion tube it
Between, the 1st refrigerant pipe that freezing machine and expansion tube are coupled together；Inner containment the 1st refrigerant pipe forms sleeve pipe, positioned at evaporation
The 2nd refrigerant pipe between machine and compressor, the two being coupled together.Compared to the length of evaporation tube, the 2nd refrigerant pipe or the 1st
The length of refrigerant pipe is 70%～130%.
To achieve these goals, may include according to the superfreeze storehouse of the embodiment of the present invention：Accommodate the steaming of evaporation tube
Send out machine, compressor, expansion tube, freezing machine, sleeve pipe.In this case, sleeve pipe includes：1st refrigerant pipe described in inner containment
Form sleeve pipe, the 2nd refrigerant pipe between rapid steamer and compressor, the two being coupled together.When cold-producing medium is in evaporation tube
Traveling time be the 1st traveling time, traveling time in the 2nd refrigerant pipe for the cold-producing medium be 2 traveling time when, by the 2nd
The length of refrigerant pipe is set as making the 2nd traveling time and the ratio of the 1st traveling time reach 70%～130%.
Invention effect
According to the present invention, the cold-producing medium discharged from freezing machine and the cold-producing medium discharged from rapid steamer are carried out the set of heat exchange
Tubular to become sleeve pipe volume compared to evaporation pipe volume be 70%～130, thus with the cooling circulating repetition of cold-producing medium, freezing
The temperature of agent can promptly be down to ultralow temperature.
Brief description
Fig. 1 is the stereogram in the superfreeze storehouse according to one embodiment of the invention.
Fig. 2 is the reference view that the refrigeration cycle to the superfreeze storehouse according to the embodiment of the present invention illustrates.
Fig. 3 and Fig. 4 is sleeve pipe one shown in Fig. 2 example with reference to figure.
Fig. 5 and Fig. 6 is disposed on the reference view of sleeve pipe between main body and body and sleeve pipe molding structure.
Fig. 7 is the reference view of the method for sleeve pipe volume of basis embodiment.
Fig. 8 is that the reference that the refrigeration cycle to the superfreeze storehouse according to another embodiment of the present invention illustrates is illustrated
Figure.
Specific embodiment
The rapid steamer mentioned in this specification is made up of evaporation tube.In this manual, rapid steamer and its implication of evaporation tube
Can use with.
Next, with reference to accompanying drawing to a preferred embodiment of the present invention will be described in detail.Here it should be noted that
Identical inscape in accompanying drawing is indicated with same symbol as far as possible.In addition, for the public affairs that present subject matter generation may be obscured
Know function and composition, be just no longer described in detail here.Based on the reason same, a part of inscape in accompanying drawing is carried out
Exaggerate or omit or diagrammatic illustration.
Fig. 1 is the stereogram in the superfreeze storehouse 100 being shown according to one embodiment of the invention, and Fig. 2 is to according to this
The reference view that the refrigeration cycle in the superfreeze storehouse 100 of inventive embodiments illustrates.
Understand referring concurrently to Fig. 1 and Fig. 2, the superfreeze storehouse 100 according to embodiment has body 103 and refrigerating chamber
101, refrigerating chamber 101 can accommodate biological tissue, blood, cell tissue.In order to externally clear the inside, refrigerating chamber 101
Window can also be set.In such case, it is contemplated that refrigerating chamber 101 temperature of -80 degree, window can be by having vacuum
The double glazing of layer is constituted.
The lower end in superfreeze storehouse 100 can accommodate freezing machine 120 and compressor 110, and the back side can accommodate sleeve pipe
140.Here, sleeve pipe 140 can accommodate the prominent form of the 1st refrigerant pipe 141 according to the 2nd refrigerant pipe 142.1st refrigeration
Agent pipe 141 is connected to expansion tube the 150, the 2nd refrigerant pipe 142 from Filter dryer 130 and can be connected to rapid steamer 160 and compression
Between machine 110.That is, the 1st refrigerant pipe 141 is used for the cold-producing medium that cooling flows to expansion tube 150 from Filter dryer 130.2nd system
Refrigerant tube 142 can cool down the cold-producing medium of the 1st refrigerant pipe 141 in advance, then again by cooling cold-producing medium to expansion tube 130 row
Go out.
After Filter dryer 130 filters moisture or foreign matter from the cold-producing medium that freezing machine 120 is discharged, then cold-producing medium is provided
The 1st refrigerant pipe 141 to sleeve pipe 140.
Here, the 1st refrigerant pipe 141 in sleeve pipe 140 makes cold-producing medium flow to expansion tube 150 from Filter dryer 130
Dynamic, the 2nd refrigerant pipe 142 makes cold-producing medium flow to compressor 110 from rapid steamer 160.That is, flow in the 1st refrigerant pipe 141
Cold-producing medium and in the 2nd refrigerant pipe 142 flowing cold-producing medium mutually inversely move, by this reverse movement, Ke Yiyou
Effect execution the 1st refrigerant pipe 141 and the heat exchange of the 2nd refrigerant pipe 142.
This sleeve pipe 140 configures behind the back side of shell 103, is molded (molding) by polyurathamc.Foam poly- ammonia
Ester is the resin that a kind of inside carries countless air layers, is coated between refrigerating chamber 101 and body 103, can make according to enforcement
The superfreeze storehouse 100 of example is heat-insulated.In this case, can be molded with planar line between body 103 and refrigerating chamber 101
The sleeve pipe 140 of loop-shaped.
In order that volume reaches minimum, and make structure compacter, sleeve pipe 140 can be formed as planar line ring.Set
Pipe 140 can have the loop shape from week facing to central part.Therefore, sleeve pipe 140 is configured behind the back side of body 103,
With polyurathamc shaping, on the premise of the thickness that will not make body 103 increases too much, can also be become by polyurathamc
Type is at the back side of body 103.This will describe in detail below.
The cold-producing medium discharged from Filter dryer 130 passes through the 2nd refrigerant pipe in the 1st refrigerant pipe 141 of sleeve pipe 140
After 142 carry out adding cooling, then provide to decompressor 150.In this case, permissible to the cold-producing medium of decompressor 150 applying
It is in by the state of sufficiently over cooling.Supercooled cold-producing medium expands in expansion tube 150, becomes low temperature/low pressure
The cold-producing medium of gaseous state, when it flows into refrigerating chamber 101, it just can drop to sufficiently low temperature.
The latent heat of rapid steamer 160 absorption refrigerating 101 makes cold-producing medium be converted to liquid condition from gas phase.In this situation
Under, rapid steamer 160 has an evaporation tube form in vaporization chamber 101 within for the configuration, the volume of sleeve pipe 140 and the volume of evaporation tube it
Than 1：In the range of 1 or 70%～130%.
Here,
1) volume of evaporation tube refers to the volume calculating on the basis of the internal diameter of evaporation tube；
2) volume of sleeve pipe 140 refers to [volume of volume-the 1 refrigerant pipe 141 of the 2nd refrigerant pipe 142].Below,
[volume of volume-the 1 refrigerant pipe 141 of the 2nd refrigerant pipe 142] is defined as " difference volume ".
In this case, the volume of the 2nd refrigerant pipe 142 corresponds on the basis of the internal diameter of the 2nd refrigerant pipe 142
Volume, and the volume of the 1st refrigerant pipe 141 corresponds to the volume on the basis of the external diameter of the 1st refrigerant pipe 141.
Here, the volume of the 2nd refrigerant pipe 142 purely refers to that cold-producing medium can flow in the inside of the 2nd refrigerant pipe 142
Dynamic internal volume.
When allosome of being on duty amasss=evaporate pipe volume, the cold-producing medium discharged to compressor 110 from evaporation tube will be from filtration drying
Device 130 flows to the liquid refrigerant cooling of expansion tube 150, is flowed to from Filter dryer 130 by the 1st refrigerant pipe 141 and expands
After the cold-producing medium of pipe 150 cools down in freezing machine 120, through cooling down again, can provide to expansion tube 150.In expansion tube 150
The cold-producing medium of vaporization is in low temperature/low-pressure state, to the 2nd refrigerant pipe after the latent heat of absorption refrigerating 101 in rapid steamer 160
142 offers.Cold-producing medium carries out heat exchange in the 2nd refrigerant pipe 142 with the 1st refrigerant pipe 141, absorbs in the 1st refrigerant pipe
After the heat of cold-producing medium of flowing in 141, compressor 110 can be returned.Therefore, compressor 110 receives and passes through the 1st refrigerant pipe
Can provide to freezing machine 120 after the cold-producing mediums of 141 heating the rapid state that refrigerant compression is become high temp/high pressure.So,
The cold-producing medium being transmitted back to compressor 110 from the 2nd refrigerant pipe 142 is sufficiently heated, and can improve compression refrigeration in compressor 110
Agent is thus be converted to the efficiency of the state of high temp/high pressure.Improve efficiency be meant to be more quickly completed cooling circulation it is possible to
Reduce the temperature of refrigerating chamber 101 further.
In this case, the volume of the 2nd refrigerant pipe 142 both can be pressed with the evaporation pipe volume constituting rapid steamer 160
According to 1：1 ratio carries out equivalent configuration it is also possible to increase and decrease to its volume according to target temperature.
The volume of evaporation tube is to the proportional relation of cooling capacity reducing refrigerating chamber 101 temperature it is assumed that according to evaporation tube
Cooling capacity configures the volume of the 2nd refrigerant pipe 142, and the refrigerant velocities one that flows to node D of from node A regularly so that it may
Heated in the 2nd refrigerant pipe 142 of same volume with the cold-producing medium being considered as in evaporation Bottomhole pressure.Therefore, from evaporation tube to
The cold-producing medium of compressor 110 flowing applies to compressor 110 after being fully warmed-up in the 2nd refrigerant pipe 142 again.Then, press
Contracting machine 110, by after the refrigerant compression of preheating, provides to freezing machine 120.The order of this warm-up cycle is compressor
110- freezing machine 120- Filter dryer 130, circulates whenever repeating the cooling to sleeve pipe 140- decompressor 150- rapid steamer 160
When, the heat of pre- warm refrigerant will accumulate, such that it is able to improve the efficiency of cooling circulation.
I.e., it is possible to make refrigerating chamber 101 be rapidly cooled to ultra low temperature state at short notice.For example：Evaporate when assuming to constitute
The caliber of the evaporation tube of machine 160 is 7mm, and the external diameter of the 1st refrigerant pipe 141 of forming sleeves 140 is 4mm, the 2nd refrigerant pipe
When 142 internal diameter is 8mm (external diameter is 9mm), the volume of evaporation tube just can be according to (radius)2X Π x h (length) is counted
Calculate, you can be calculated according to " 12.25 Π x h ".
In this case, the volume of the 1st refrigerant pipe 141 is " 4 Π x h ", and the volume of the 2nd refrigerant pipe 142 is permissible
Calculated according to " 16 Π x h ", difference volume can be calculated according to " 16 Π x h " " 4 Π x h "=" 12 Π x h ".
If it is assumed that the equal length of the length of evaporation tube and the 2nd refrigerant pipe 142, then with respect to the 2nd cold-producing medium of evaporation pipe volume
The volume ratio of pipe 142 (or the 1st refrigerant pipe 141) is calculated as 12/12.5=96%.
In addition, when the evaporation pipe volume being determined by described volume ratio and the 2nd refrigerant pipe 142 (or the 1st refrigerant pipe 141)
Volume close when, to expansion tube 150 flow into refrigerant temperature rise in the presence of the 1st refrigerant pipe 141, by the 2nd
Refrigerant pipe 142 declines to the refrigerant temperature that compressor 110 flows from evaporation tube.In this course, with expansion tube 150
The expansion temperature difference (Δ T) of the temperature difference definition between the outside air temperature of the refrigerant temperature of interior expansion and refrigerating chamber 101 declines.
Expand the temperature difference (Δ T) decline make the refrigerant temperature in evaporation Bottomhole pressure be unlikely to be reduced to -100 DEG C with
Under, the temperature of cold-producing medium can be made to reach -70 DEG C～-80 DEG C.That is, can be rapidly reached according to the superfreeze storehouse of embodiment
Certain temperature range (- 70 DEG C～-80 DEG C), it is not so that temperature is reduced or raise, but can be rapid
Reach the temperature range (- 70 DEG C～-80 DEG C) of regulation.According to embodiment medical freezer can by cell, DNA, blood and
Other materials preserving for experiment or needs are preserved rapidly within the scope of certain temperature.
Fig. 3 and Fig. 4 be illustrate sleeve pipe 140 1 shown in Fig. 2 example with reference to figure.Next, with reference to Fig. 1 to Fig. 3 and Fig. 4
Illustrate.
From figure 3, it can be seen that the sleeve pipe 140 according to embodiment is in planar line round, wherein insert the 1st refrigerant pipe
One face of 141 the 2nd refrigerant pipe 142 forms concentric circles from side face to central part.For this structure, when according to real
The sleeve pipe 140 applying example configures when the back side of body 103, is just attached to body 103 back side with the shape of planar coil, thus can
Not increase the thickness of body 103.I.e., it is possible to make according to embodiment superfreeze storehouse structure compacter, thin.Fig. 3
The side of shown sleeve pipe 140 can be connected with Filter dryer 130, opposite side can from central part to D4 direction prominent and with swollen
Tube expansion 150 connects.
As shown in figure 4, the back side of main body 103-1 is close to by sleeve pipe 140, expose the concentric structure of plane to outside.?
Under this state, body 103 is enclosed within main body 103-1, if being coated with polyurathamc between body 103 and main body 103-1
Resin just can complete forming operation.In this regard, will illustrate with reference to Fig. 5 and Fig. 6.
First, Fig. 5 shows and sleeve pipe 140 configures an example in main body 103-1.It can be seen that
Sleeve pipe 140 and the exposure configured in parallel of main body 103-1, will not increase the thickness of main body 103-1.Fig. 6 is to illustrate to be configured with set
Configuration relation between main body 103-1 of pipe 140 and body 103 with reference to figure, as shown in fig. 6, sleeve pipe 140 is configured in main body
After 103-1 is upper, can be to region the S1 filling such as the heat-barrier material of polyurathamc etc. between main body 103-1 and body 103.?
Although refer to the heat-barrier material as filling region S1 with polyurathamc in the present embodiment, but, in addition, also may be used
With the heat-barrier material filling region S1 with expanded polystyrene (EPS) or bipeltate and other various material.
If filling region S1 with polyurathamc, sleeve pipe 140 in main body 103-1 for the configuration just can be poly- by foaming
Urethane is molded together with body 103.Therefore, sleeve pipe 140 will not be affected by external temperature, and realize the 1st refrigerant pipe 141 with
Heat exchange between 2nd refrigerant pipe 142.
Fig. 7 show the method for sleeve pipe 140 volume of basis embodiment with reference to figure.
Understand with reference to Fig. 7, calculate the on the basis of the outer diameter D 2 of the 1st refrigerant pipe 141 according to the sleeve pipe 140 of embodiment
The volume of 1 refrigerant pipe 141, for the 2nd refrigerant pipe 142, calculates the 2nd refrigerant pipe 142 on the basis of internal diameter D2
Volume.Meanwhile, the refrigerant volume of flowing in the 2nd refrigerant pipe 142 can be calculated as the body of the 1st refrigerant pipe 141
The difference of the long-pending volume with the 2nd refrigerant pipe 142 is volume differences.
The volume of round tubular structure can be calculated by following mathematical expressions 1, on this basis it is possible to calculate
The volume of the 1st refrigerant pipe 141, the volume of the 2nd refrigerant pipe 142 and volume differences.
V=π × r2×h
Here, v represents the volume of cylinder, and Π represents pi, and r represents the radius of cylinder, and h represents the length of cylinder.
Understand, the volume of the 1st refrigerant pipe 141 can be calculated by following mathematical expressions 2 with reference to mathematical expression 1.
Here, v1 represents the volume of the 1st refrigerant pipe 141, and Π represents pi, and D1 represents the 1st refrigerant pipe 141
Radius, H represents the length of the 1st refrigerant pipe 141.
It is then possible to calculate the volume of the 2nd refrigerant pipe 142 with reference to mathematical expression 1 and by following mathematical expressions 3.
Here, v2 represents the volume of the 2nd refrigerant pipe 142, and Π represents pi, and D2 represents the half of the 2nd refrigerant pipe
Footpath, H represents the length of the 2nd refrigerant pipe 142.In this case, D2 can represent the internal diameter radius of the 2nd refrigerant pipe 142.
This is because, calculate the volume differences between the internal volume of the 2nd refrigerant pipe 142 and the external volume of the 1st refrigerant pipe 141
Afterwards, can use it for calculating the pure volume of the 2nd refrigerant pipe 142.
Difference volume can be calculated by V2-V1.Length can be adjusted, so that according to described mathematical expression 1～mathematics
The difference volume that formula 3 calculates reaches 70%～130% with the ratio of the volume of evaporation tube.Allosome of being on duty amasss=evaporation pipe volume
When it is possible to evaporation Bottomhole pressure cold-producing medium be fully warmed-up.Allosome of being on duty is amassed and is exceeded with the ratio evaporating pipe volume
Additionally it is possible to be preheated further when 100%.If the refrigerated storage temperature according to the superfreeze storehouse of embodiment can not drop
Following to -80 degree, then can be 70%～100% compared to the difference volume of evaporation pipe volume.On the contrary, if according to embodiment
Ultra low temperature freezer require cool to -80 degree below temperature, then compared to evaporation pipe volume difference volume can be 101%
～130%.That is, can be incited somebody to action according to the superfreeze storehouse according to embodiment with respect to the ratio of the difference volume of evaporation pipe volume
Which kind of degree is the temperature of refrigerating chamber 101 be reduced to determines.
If the equal length of the length of evaporation tube and the 2nd refrigerant pipe 142, this means that the volume of evaporation tube and the
The difference volume of 2 refrigerant pipes 142 and the 1st refrigerant pipe 141 is equal.In this case, according to the ultra-low temperature cold of embodiment
Freezing the length of the 2nd refrigerant pipe 142 and the length ratio of evaporation tube in storehouse 100 is 70%～130%.
Fig. 8 is the reference picture that the refrigeration cycle to the superfreeze storehouse according to another embodiment of the present invention illustrates.
Understand with reference to Fig. 8, according to the refrigeration cycle in superfreeze storehouse and the situation phase being illustrated by Fig. 2 of embodiment
Same, there is the refrigeration cycle of compression condensation-expansion-evaporation.Eliminate a part of structure in detail in this figure, but identical with Fig. 2, with
With compressor 110, freezing machine 120, Filter dryer 130, sleeve pipe 140, expansion tube 150 and rapid steamer 160 ultra-low temperature cold
Freeze storehouse corresponding.
Therefore, compressor 110, freezing machine 120, Filter dryer 130 and the expansion tube 150 repeating with structure shown in Fig. 2
Just it will not be described and diagram, is referred to Fig. 2 to the explanation of these inscapes and understands.
This embodiment is characterized in that, it is not the volume using the evaporation tube constituting rapid steamer 160, but utilize cold-producing medium
In traveling time and the ratio of the time of movement in the 2nd refrigerant pipe 142 of evaporation in-pipe, make in the 2nd refrigerant pipe
The cold-producing medium of movement provides to compressor 100 after fully absorbing heat again.So, it is recycled to pressure after making refrigerant heat again
Contracting machine 100, thus when compressor 100 is compressed to cold-producing medium, the State Transferring that can make cold-producing medium at short notice is
There is provided to freezing machine 120 again after high temp/high pressure state.When cold-producing medium through freezing machine 120 to expansion tube 150 mobile when so as to
Cool down in the 1st refrigerant pipe 141, such that it is able to make cold-producing medium heat in the 2nd refrigerant pipe 142, and in the 1st refrigerant pipe
Carry out sub-cooled in 141.If heating and the sub-cooled of cold-producing medium are repeated, according to the superfreeze of embodiment
The temperature of refrigerating chamber 101 just can be down to -80 degree or lower temperature by storehouse at short notice.Here, with cold-producing medium plus
The item of heat and sub-cooled correlation is not exclusively applicable for structure shown in Fig. 8, is applicable to the present embodiment overall.
System compared to the 1st traveling time t1 movement in the 2nd refrigerant pipe 142 of the cold-producing medium in evaporation in-pipe
2nd traveling time t2 of cryogen can be 70%～130%.Performance according to freezing machine 120 will be it is also possible to will move compared to the 1st
The 2nd traveling time t2 of dynamic time t1 increases to more than 70%～130% scope.
In addition, the embodiments of the invention enumerated in the specification and drawings are to the present invention in order to more easy-to-understand
Technology contents illustrate, and the particular example contributing to the understanding of the present invention and enumerating, it does not limit the present invention's
Scope.Certainly, in addition to the embodiment enumerated here, those skilled in the art completely can be with the skill of the present invention
To implement other variation based on art thought.
Industrial applicability
Industry and gene that the present invention for medical industries, can be taken care of, studied and be operated to blood or cell tissue
Operation industry is made contributions, if used it for abiotic tissue (such as：Article or material) long-term keeping when it is also possible to
Be freezing and keeping industry make contributions.
Claims (11)
1. a kind of superfreeze storehouse it is characterised in that：
This superfreeze storehouse has：Rapid steamer with evaporation tube；Compressor；Expansion tube；And freezing machine,
And include：Described freezing machine and described expansion tube are coupled together between described freezing machine and described expansion tube by configuration
1st refrigerant pipe；
1st refrigerant pipe described in inner containment is thus form sleeve pipe, and is connected between described rapid steamer and described compressor
2nd refrigerant pipe；
Difference compared to the volume of volume and described 1st refrigerant pipe of described 2nd refrigerant pipe of the volume of described evaporation tube
I.e. difference volume is 70%～130%.
2. superfreeze storehouse according to claim 1 it is characterised in that：
Described difference volume refer to for the 1st volume being calculated based on the external diameter of described 1st refrigerant pipe with based on the described 2nd
The volume differences of the 2nd volume that the internal diameter of refrigerant pipe calculates.
3. superfreeze storehouse according to claim 1 it is characterised in that：
Described 1st refrigerant pipe is reverse each other with the moving direction of the cold-producing medium of described 2nd refrigerant pipe.
4. superfreeze storehouse according to claim 1 it is characterised in that：
This superfreeze storehouse also includes：Configuration, will be from described freezing machine between described 1st refrigerant pipe and described freezing machine
Moisture in the cold-producing medium discharged and the Filter dryer of foreign matter removing.
5. superfreeze storehouse according to claim 1 it is characterised in that：
Described 2nd refrigerant pipe is formed as the planar coil form to central part from side face, described central part project and with described
Expansion tube links together.
6. superfreeze storehouse according to claim 1 it is characterised in that：
Described 2nd refrigerant pipe has the length equal with described evaporation tube, in this case, described difference volume with described
The internal diameter volume of evaporation tube is equal.
7. superfreeze storehouse according to claim 1 it is characterised in that：
Described 2nd refrigerant pipe polyurathamc is molded.
8. a kind of superfreeze storehouse it is characterised in that：
This superfreeze storehouse has：Rapid steamer with evaporation tube, compressor, expansion tube and freezing machine,
And include：Described freezing machine and described expansion tube are coupled together between described freezing machine and described expansion tube by configuration
1st refrigerant pipe；
1st refrigerant pipe described in inner containment forms sleeve pipe, and is connected to the 2nd system between described rapid steamer and described compressor
Refrigerant tube；
If the cold-producing medium traveling time in described evaporation tube is the 1st traveling time, described in described 2nd refrigerant pipe
When cold-producing medium traveling time is 2 traveling time, just by the length of described 2nd refrigerant pipe according to mobile compared to the described 1st
Described 2nd traveling time of time is that 70%～130% standard is set.
9. superfreeze storehouse according to claim 8 it is characterised in that：
Described 1st refrigerant pipe is reverse each other with the moving direction of the cold-producing medium of described 2nd refrigerant pipe.
10. superfreeze storehouse according to claim 8 it is characterised in that：
This superfreeze storehouse also includes：Configuration, will be from described freezing machine between described 1st refrigerant pipe and described freezing machine
Moisture in the cold-producing medium discharged and the Filter dryer of foreign matter removing.
11. superfreeze storehouses according to claim 8 it is characterised in that：
Described 2nd refrigerant pipe is formed as the planar coil form to central part from side face, described central part project and with described
Expansion tube links together.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020140060685A KR101438155B1 (en) | 2014-05-21 | 2014-05-21 | Ultra low temperature freezer |
| KR10-2014-0060685 | 2014-05-21 | ||
| PCT/KR2015/004994 WO2015178659A1 (en) | 2014-05-21 | 2015-05-19 | Ultra low temperature freezer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106461286A true CN106461286A (en) | 2017-02-22 |
Family
ID=51759476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201580025533.8A Pending CN106461286A (en) | 2014-05-21 | 2015-05-19 | Ultra low temperature freezer |
Country Status (3)
| Country | Link |
|---|---|
| KR (1) | KR101438155B1 (en) |
| CN (1) | CN106461286A (en) |
| WO (1) | WO2015178659A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101962316B1 (en) | 2017-02-01 | 2019-03-26 | 주식회사 일신바이오베이스 | Cryogenic freezer |
| KR101949090B1 (en) * | 2018-07-31 | 2019-02-15 | 주식회사 지엠에스 | deep freezer using induction pipe |
| KR102024241B1 (en) * | 2018-10-25 | 2019-09-23 | 윤근진 | Cryogenic Freezer |
| KR101977901B1 (en) * | 2018-12-17 | 2019-08-28 | 윤근진 | Cryogenic Freezer |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02140170U (en) * | 1989-04-19 | 1990-11-22 | ||
| JP2006170571A (en) * | 2004-12-17 | 2006-06-29 | Hitachi Cable Ltd | Double multitubular heat exchanger |
| CN101210783A (en) * | 2006-12-28 | 2008-07-02 | 株式会社科倍可菱材料 | Heat exchanger |
| CN101280974A (en) * | 2007-04-06 | 2008-10-08 | 三星电子株式会社 | Refrigerant cycle device |
| CN102080903A (en) * | 2009-11-30 | 2011-06-01 | 三洋电机株式会社 | Refrigerating apparatus |
| CN103090602A (en) * | 2011-11-08 | 2013-05-08 | 三星电子株式会社 | Non-azeotropic mixed refrigerant cycle and refrigerator equipped therewith |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR19990080927A (en) * | 1998-04-23 | 1999-11-15 | 신영주 | Automotive Cooling System |
| JP4062129B2 (en) * | 2003-03-05 | 2008-03-19 | 株式会社デンソー | Vapor compression refrigerator |
-
2014
- 2014-05-21 KR KR1020140060685A patent/KR101438155B1/en active IP Right Grant
-
2015
- 2015-05-19 CN CN201580025533.8A patent/CN106461286A/en active Pending
- 2015-05-19 WO PCT/KR2015/004994 patent/WO2015178659A1/en active Application Filing
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02140170U (en) * | 1989-04-19 | 1990-11-22 | ||
| JP2006170571A (en) * | 2004-12-17 | 2006-06-29 | Hitachi Cable Ltd | Double multitubular heat exchanger |
| CN101210783A (en) * | 2006-12-28 | 2008-07-02 | 株式会社科倍可菱材料 | Heat exchanger |
| CN101280974A (en) * | 2007-04-06 | 2008-10-08 | 三星电子株式会社 | Refrigerant cycle device |
| CN102080903A (en) * | 2009-11-30 | 2011-06-01 | 三洋电机株式会社 | Refrigerating apparatus |
| CN103090602A (en) * | 2011-11-08 | 2013-05-08 | 三星电子株式会社 | Non-azeotropic mixed refrigerant cycle and refrigerator equipped therewith |
Also Published As
| Publication number | Publication date |
|---|---|
| KR101438155B1 (en) | 2014-09-05 |
| WO2015178659A1 (en) | 2015-11-26 |
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