CN206831877U - Biochemical instruments refrigerating plant - Google Patents
Biochemical instruments refrigerating plant Download PDFInfo
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- CN206831877U CN206831877U CN201720254266.8U CN201720254266U CN206831877U CN 206831877 U CN206831877 U CN 206831877U CN 201720254266 U CN201720254266 U CN 201720254266U CN 206831877 U CN206831877 U CN 206831877U
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- China
- Prior art keywords
- chill plate
- biochemical instruments
- refrigerating plant
- type evaporator
- inflation type
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Abstract
The utility model provides a kind of biochemical instruments refrigerating plant, including the chill plate for cooling down biochemical instruments reagent disc, the refrigeration module being set in outside chill plate, and at least one inflation type evaporator for being set in chill plate inner chamber, each inflation type evaporator are coaxially disposed with chill plate and are connected with refrigeration module by circulation pipe.The utility model can realize the cooling to biochemical instruments reagent disc.Because inflation type evaporator can complete refrigerating function, chill plate is no longer refrigeration generating body, and therefore, the manufacture material of chill plate uses the material of poor thermal conductivity, while its processing technology requires to reduce.In addition the manufacturing process of inflation type evaporator is extremely ripe, and manufacturing cost is low.In addition, the parts of the biochemical instruments refrigerating plant are structural member, its fault rate is low, easily maintenance.
Description
Technical field
Cooling technology field is the utility model is related to, more particularly to a kind of biochemical instruments refrigerating plant.
Background technology
The storage temperature requirement of biochemical instruments reagent disc at 2 DEG C~8 DEG C, it is general to the type of cooling of chill plate at present use with
Lower three kinds：
1st, by the way that coolant is circulated so as to realize the cooling to biochemical instruments reagent disc in double-deck chill plate, due to this
Mode needs to process a double-deck chill plate and the processing technology of double-deck chill plate is more complicated, so that cooling cost becomes
It is high.
2nd, the chill plate for installing biochemical instruments reagent disc is directly cooled down by semiconductor refrigeration chip, this mode is only
Low capacity chill plate is only applicable to, the cooling for Large Copacity chill plate then needs much to organize semiconductor refrigeration chip, it is necessary to very
High power could maintain the normal work of multigroup chip.This kind of type of cooling causes cooling cost to uprise, in addition Large Copacity system
The manufacturing cost of cold dish is also very high, therefore the integrated cost of this kind of type of cooling is very high.
3rd, freezed by cold wind, cold wind circulated in chill plate, this type of cooling due to refrigeration servicing unit more than from
And make it that working link is more, system is more complicated, and cooling cost is very high.
The content of the invention
In view of the above the shortcomings that prior art, the technical problems to be solved in the utility model is to provide a kind of biochemistry
Instrument refrigerating plant, biochemical instruments reagent disc can be cooled down, simple in construction, easy to manufacture, cooling cost is low.
In order to solve the above-mentioned technical problem, the utility model provides a kind of biochemical instruments refrigerating plant, including for cooling down life
Change the chill plate of instrument reagent disc, the refrigeration module being set in outside chill plate, and at least one be set in blowing for chill plate inner chamber
Expanding evaporator, each inflation type evaporator are coaxially disposed with chill plate and are connected with refrigeration module by circulation pipe.
Preferably, the outer wall cladding heat-insulation layer of the chill plate.
Preferably, the heat-insulation layer is made up of heat-preservation cotton.
Preferably, each inflation type evaporator includes the evaporation plectane being coaxially disposed with the chill plate, is formed at
Evaporate the circulation line in plectane, the water inlet pipe being connected with the entrance point of circulation line, and the port of export phase with circulation line
Outlet pipe even, water inlet pipe and outlet pipe form the circulation pipe and are connected with the refrigeration module.
Preferably, the periphery of the evaporation plectane is provided with several first breach, the inwall of the chill plate provided with it is every
The individual one-to-one installation portion of first breach, the evaporation plectane by be arranged on the first fixture of each first indentation, there with
The installation portion is fixedly linked.
Preferably, the evaporation plectane has centre bore, and the inwall of centre bore is provided with several second breach, described
The bottom centre of chill plate has an annular table, the evaporation plectane by be arranged on the second fixture of each second indentation, there with
The annular table is fixedly linked.
Preferably, the circulation line is in the shape of a spiral.
Preferably, the quantity of the inflation type evaporator is one, and inflation type evaporator is set in the bottom of chill plate.
Preferably, the chill plate is made of plastics.
As described above, biochemical instruments refrigerating plant of the present utility model, has the advantages that：
1st, the utility model can cool down to biochemical instruments reagent disc, simple in construction, and easy to manufacture, cooling cost is low.
2nd, the manufacture material of chill plate uses the material of poor thermal conductivity, while its processing technology requires to reduce.
3rd, the utility model reduces the thickness of heat-insulation layer, and the cladding work of heat-insulation layer becomes easy.
Brief description of the drawings
Fig. 1 is shown as the explosive view of biochemical instruments refrigerating plant of the present utility model.
Fig. 2 is shown as the top view of biochemical instruments refrigerating plant of the present utility model.
Fig. 3 is shown as the sectional view of biochemical instruments refrigerating plant of the present utility model.
Component label instructions
1 inflation type evaporator
11 evaporation plectanes
12 circulation lines
13 outlet pipes
14 water inlet pipes
15 first breach
16 second breach
2 chill plates
21 installation portions
22 annular tables
3 heat-insulation layers
Embodiment
Embodiment of the present utility model is illustrated by particular specific embodiment below, those skilled in the art can be by this
Content disclosed by specification understands other advantages and effect of the present utility model easily.
Fig. 1 to Fig. 3 is referred to it should be clear that structure depicted in this specification institute accompanying drawing, ratio, size etc., only to
Coordinate the content disclosed in specification, so that those skilled in the art understands and reads, be not limited to the utility model
Enforceable qualifications, therefore do not have technical essential meaning, the modification of any structure, the change of proportionate relationship or size
Adjustment, in the case where not influenceing the effect of the utility model can be generated and the purpose that can reach, all should still fall in the utility model
In the range of disclosed technology contents can be covered.Meanwhile in this specification it is cited as " on ", " under ", " left side ",
The term on " right side ", " centre " and " one " etc., understanding for narration is merely convenient to, and it is enforceable to be not used to restriction the utility model
Scope, its relativeness are altered or modified, enforceable when being also considered as the utility model in the case where changing technology contents without essence
Category.
As shown in figure 1, the utility model provides a kind of biochemical instruments refrigerating plant, including for cooling down biochemical instruments reagent disc
Chill plate 2, the refrigeration module being set in outside chill plate, and at least one inflation type evaporator 1 for being set in chill plate inner chamber,
Each inflation type evaporator 1 is coaxially disposed with chill plate 2 and is connected with refrigeration module by circulation pipe.
In above-described embodiment, the coolant through refrigeration module cooling flows into inflation type evaporator 1 by circulation pipe, with refrigeration
After the air of disk inner chamber carries out heat exchange, then refrigeration module flow back into by circulation pipe, complete the refrigeration to chill plate inner chamber, from
And realize the cooling to biochemical instruments reagent disc.Because inflation type evaporator 1 can complete refrigerating function, chill plate 2 is no longer system
Cold generating body, therefore, the manufacture material of chill plate 2 use the material of poor thermal conductivity, and its processing technology requires to reduce, so as to cool down
Cost reduces.In addition the manufacturing process of inflation type evaporator 1 is extremely ripe, simple in construction, easy to manufacture.In addition, the biochemical instruments
The parts of refrigerating plant are structural member, and its fault rate is low, easily maintenance.
As shown in figure 3, in order to further improve the cooling effect of biochemical instruments refrigerating plant, the outer wall cladding of chill plate 2 is protected
Warm layer 3.Because chill plate 2 employs the material of poor thermal conductivity, thus reduce the thickness of heat-insulation layer 3, the cladding work of heat-insulation layer 3
Work becomes easy.
Because heat-preservation cotton is a kind of good heat preserving and insulating material, therefore heat-insulation layer 3 is made up of heat-preservation cotton.In addition, insulation
Cotton is a kind of nontoxic, harmless, free of contamination insulation material, can directly be contacted with human body skin, therefore staff is cooling down
, will not be by any adverse effect in operating process.
As shown in Fig. 2 each inflation type evaporator 1 includes the evaporation plectane 11 being coaxially disposed with chill plate 2, steaming is formed at
Send out plectane 11 in circulation line 12, the water inlet pipe 14 being connected with the entrance point of circulation line 12, and with circulation line 12
The connected outlet pipe 13 of the port of export, water inlet pipe 14 and outlet pipe 13 form circulation pipe and are connected with refrigeration module.Inflation type evaporator 1
Using evaporation plectane 11, in order that the outline of inflation type evaporator 1 matches with chill plate inner chamber, installing/dismounting is more convenient.
The water inlet pipe 14 and outlet pipe 13 of inflation type evaporator 1 pass sequentially through the side disengaging of chill plate 2 and heat-insulation layer 3
Mouth stretches out to be connected with refrigeration module.Because water inlet pipe 14 and outlet pipe 13 can not import and export blind-mate with side, therefore need
Good seal is imported and exported into the side of chill plate 2 and heat-insulation layer 3 with rubber filling thing.Water inlet pipe 14 passes through silicone tube and refrigeration mould
The outlet of block is connected, and outlet pipe 13 is connected also by silicone tube with the import of refrigeration module, inflation type evaporator 1 and refrigeration module
Collectively form the circulatory system of coolant.
The cyclic process of coolant：Coolant is cooled down by refrigeration module first, then flows into inflation type by water inlet pipe 14
The circulation line 12 of evaporator 1, heat exchange is then carried out by inflation type evaporator 1 and the air of chill plate inner chamber, finally led to
Cross outlet pipe 13 and flow back to refrigeration module, complete the refrigeration to chill plate inner chamber, so as to realize the cooling to biochemical instruments reagent disc.
As shown in Figure 1 and Figure 2, in order to prevent the play in chill plate inner chamber of inflation type evaporator 1, the outer of plectane 11 is evaporated
It is provided with several first breach 15 week, the inwall of chill plate 2 is provided with and the one-to-one installation portion 21 of each first breach 15, steaming
Hair plectane 11 is fixedly linked by being arranged on the first fixture of each first indentation, there with installation portion 21.In the specific implementation,
Plectane 11 circumference array, six the first breach 15 are evaporated, evaporation plectane 11 is by being arranged on the screw and peace of each first indentation, there
Dress portion 21 is fixedly linked.
As shown in Figure 1 and Figure 2, in order to further reinforce the connection of inflation type evaporator 1 and chill plate 2, evaporation plectane 11 has
There is centre bore, and the inwall of centre bore is provided with several second breach 16, the bottom centre of chill plate 2 has annular table 22,
Evaporation plectane 11 is fixedly linked by being arranged on the second fixture of each second indentation, there with annular table 22.It is being embodied
When, plectane 11 circumference array, three the second breach 16 are evaporated, evaporation plectane 11 is by being arranged on the screw of each second indentation, there
It is fixedly linked with annular table 22.
As shown in Fig. 2 circulation line 12 is in the shape of a spiral, the coolant that can so extend in circulation line 12 is in chill plate
Flowing time in inner chamber, coolant and the air of chill plate inner chamber is set to carry out sufficient heat exchange, so as to strengthen cooling effect.
As shown in figure 3, in order to both can guarantee that cooling effect, and can simplifies structure, and the quantity of inflation type evaporator 1 is one
It is individual, and inflation type evaporator 1 is set in the bottom of chill plate 2.
In order to reduce manufacturing cost, technology difficulty is reduced, chill plate 2 is made of plastics.
In summary, the utility model can cool down to biochemical instruments reagent disc, and simple in construction, cooling cost is low.Institute
So that the utility model effectively overcomes various shortcoming of the prior art and has high industrial utilization.
Above-described embodiment only illustrative principle of the present utility model and its effect are new not for this practicality is limited
Type.Any person skilled in the art can all be carried out without prejudice under spirit and scope of the present utility model to above-described embodiment
Modifications and changes.Therefore, such as those of ordinary skill in the art without departing from the essence disclosed in the utility model
God and all equivalent modifications completed under technological thought or change, should be covered by claim of the present utility model.
Claims (9)
- A kind of 1. biochemical instruments refrigerating plant, it is characterised in that：Including the chill plate (2) for cooling down biochemical instruments reagent disc, install Refrigeration module outside chill plate, and at least one inflation type evaporator (1) for being set in chill plate inner chamber, each inflation type Evaporator (1) is coaxially disposed with chill plate (2) and is connected with refrigeration module by circulation pipe.
- 2. biochemical instruments refrigerating plant according to claim 1, it is characterised in that：The outer wall cladding of the chill plate (2) is protected Warm layer (3).
- 3. biochemical instruments refrigerating plant according to claim 2, it is characterised in that：The heat-insulation layer (3) is made up of heat-preservation cotton.
- 4. biochemical instruments refrigerating plant according to claim 1, it is characterised in that：Each inflation type evaporator (1) bag The evaporation plectane (11) being coaxially disposed with the chill plate (2) is included, the circulation line (12) being formed in evaporation plectane (11), with The connected water inlet pipe (14) of the entrance point of circulation line (12), and the outlet pipe being connected with the port of export of circulation line (12) (13), water inlet pipe (14) and outlet pipe (13) form the circulation pipe and are connected with the refrigeration module.
- 5. biochemical instruments refrigerating plant according to claim 4, it is characterised in that：The periphery of the evaporation plectane (11) is provided with Several first breach (15), the inwall of the chill plate (2) are provided with and the one-to-one installation portion of each first breach (15) (21), the evaporation plectane (11) is fixed by the first fixture and the installation portion (21) for being arranged on each first indentation, there It is connected.
- 6. biochemical instruments refrigerating plant according to claim 4, it is characterised in that：The evaporation plectane (11) has center Hole, and the inwall of centre bore is provided with several second breach (16), the bottom centre of the chill plate (2) has annular table (22), the evaporation plectane (11) is fixed by the second fixture and the annular table (22) for being arranged on each second indentation, there It is connected.
- 7. biochemical instruments refrigerating plant according to claim 4, it is characterised in that：The circulation line (12) is in the shape of a spiral.
- 8. biochemical instruments refrigerating plant according to claim 1, it is characterised in that：The quantity of the inflation type evaporator (1) For one, and inflation type evaporator (1) is set in the bottom of chill plate (2).
- 9. biochemical instruments refrigerating plant according to claim 1, it is characterised in that：The chill plate (2) is made of plastics.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720254266.8U CN206831877U (en) | 2017-03-15 | 2017-03-15 | Biochemical instruments refrigerating plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720254266.8U CN206831877U (en) | 2017-03-15 | 2017-03-15 | Biochemical instruments refrigerating plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206831877U true CN206831877U (en) | 2018-01-02 |
Family
ID=60779374
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720254266.8U Active CN206831877U (en) | 2017-03-15 | 2017-03-15 | Biochemical instruments refrigerating plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206831877U (en) |
-
2017
- 2017-03-15 CN CN201720254266.8U patent/CN206831877U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20191217 Address after: 201108 Lane 152, 468, Beihengsha River Road, Minhang District, Shanghai Co-patentee after: ZHEJIANG LANYI PHARMACEUTICAL CO., LTD. Patentee after: Lanyi Technology Group Co., Ltd. Address before: 201600 floor 3 and 4, building 31, No. 116, CHEYANG Road, Chedun Town, Songjiang District, Shanghai Patentee before: Shanghai Fu Fu biological medical technology Co., Ltd. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201118 Address after: Building 3, No.152, Lane 468, North hengshahe Road, Minhang District, Shanghai, 201100 Patentee after: SHANGHAI DEFU BIOLOGICAL MEDICAL TECHNOLOGY Co.,Ltd. Address before: 201108 Lane 152, 468, Beihengsha River Road, Minhang District, Shanghai Patentee before: AILEX TECHNOLOGY GROUP Co.,Ltd. Patentee before: ZHEJIANG AILEX PHARMACEUTICAL Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201208 Address after: 201108 Lane 152, 468, Beihengsha River Road, Minhang District, Shanghai Patentee after: AILEX TECHNOLOGY GROUP Co.,Ltd. Patentee after: ZHEJIANG AILEX PHARMACEUTICAL Co.,Ltd. Address before: Building 3, No.152, Lane 468, North hengshahe Road, Minhang District, Shanghai, 201100 Patentee before: SHANGHAI DEFU BIOLOGICAL MEDICAL TECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211208 Address after: 201108 Lane 152, 468, Beihengsha River Road, Minhang District, Shanghai Patentee after: AILEX TECHNOLOGY GROUP Co.,Ltd. Patentee after: ZHEJIANG AILEX MEDICAL Co.,Ltd. Patentee after: Lanyi (Hunan) Medical Instrument Co.,Ltd. Address before: 201108 Lane 152, 468, Beihengsha River Road, Minhang District, Shanghai Patentee before: AILEX TECHNOLOGY GROUP Co.,Ltd. Patentee before: Zhejiang Lanyi Pharmaceutical Co., Ltd |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220620 Address after: 410201 No. 101-14, building 1, military civilian integration technology city, No. 769, Qingzhuhu Road, Qingzhuhu street, Kaifu District, Changsha City, Hunan Province Patentee after: Lanyi (Hunan) Medical Instrument Co.,Ltd. Address before: 201108 Lane 152, 468, Beihengsha River Road, Minhang District, Shanghai Patentee before: AILEX TECHNOLOGY GROUP Co.,Ltd. Patentee before: ZHEJIANG AILEX MEDICAL Co.,Ltd. Patentee before: Lanyi (Hunan) Medical Instrument Co.,Ltd. |
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| TR01 | Transfer of patent right |