CN202995505U - Temperature control system - Google Patents

Abstract

The utility model provides a temperature control system, which includes a cooling module, a sample chamber, a heating module and a control module; wherein the cooling module, the sample chamber and the heating module are stacked in sequence, and the control module collects the The temperature of the sample chamber is controlled, and the temperature of the cooling module and the heating module are controlled; the cooling module, the sample chamber and the heating module are all made of light-transmitting materials. The temperature control system provided by the utility model has a simple structure and is easy to integrate into other systems. The cooling module, sample chamber and heating module all use light-transmitting materials, so chemical reactions and material forms can be observed without customizing light inlet holes. specific process of change.

Description

a temperature control system

technical field

The utility model relates to the field of temperature control, in particular to a temperature control system.

Background technique

Temperature is an important factor affecting chemical reactions and changes in material form, and chemical reactions and changes in material forms in certain fields also need to record their specific processes in real time under a microscope. For example, in the field of low-temperature biomedicine, it is often necessary to observe and record information such as the volume change of cells or biological tissues during freezing and rewarming, as well as during the process of adding and removing cryoprotectants. This information is especially important for optimizing the cryopreservation of cells and tissues. , by recording the volume change of cells under different heating and cooling rates and different concentrations of cryoprotectants, and then according to the measured data, combined with relevant mathematical models, to fit the specific biophysical parameters of the cells, so as to formulate Specific cryopreservation protocols.

At present, perfusion microscopy is often used to observe the specific process of chemical reactions and material form changes. However, the cooling module of the temperature control system of the perfusion microscope is usually made of opaque metal materials (such as aluminum, copper, etc.), and the heating module is usually made of electrothermal film. When the temperature control system is used with the microscope, both the cooling module and the heating module need to be customized The light inlet is not only complicated in process, but also has an extremely limited effective field of view. It is difficult to fully understand the specific process of reaction or material form change during observation.

Furthermore, since the electrothermal film used in the perfusion microscope is composed of polyimide thin layer with embedded resistance wire, the heat is conducted outward from the center of the resistance wire, so the temperature distribution on the surface of the electrothermal film is uneven, thus cause uneven heating.

In addition, commercial freeze-drying benches are also widely used to observe changes in sample morphology. Since the sample is in a closed environment, it is not possible to dynamically add drugs to the sample area, that is, it cannot be achieved when a specific temperature and solution components change at the same time. Observe the shape changes of the samples. And the temperature collected by the temperature sensor of the freeze-drying station is the temperature on the surface of the cooling module, not the temperature around the sample, which cannot clearly indicate the actual temperature of the sample.

Utility model content

The utility model provides a temperature control system. The temperature control system has a simple structure and is beneficial to clearly observing the specific process of chemical reaction and material form change.

In order to realize the purpose of the utility model, the temperature control system proposed by the utility model includes:

cooling module, sample chamber, heating module and control module; wherein

The cooling module, the sample chamber and the heating module are stacked sequentially, the control module collects the temperature of the sample chamber, and controls the temperature of the cooling module and the heating module;

The cooling module, the sample chamber and the heating module all use light-transmitting materials.

Preferably, the sample chamber has at least one input port and at least one output port.

Further, the input port and the output port of the sample chamber pass through the cooling module or the heating module.

Preferably, the material of the cooling module is one or more of polymethyl methacrylate, polycarbonate, polyethylene terephthalate, and acrylonitrile-butadiene-styrene.

Preferably, the material of the sample cavity is one or more of polydimethylsiloxane, polyimide, polymethyl methacrylate, parylene and polytetrafluoroethylene.

Preferably, the material of the heating module is conductive glass.

Preferably, the control module includes a temperature sensor, a refrigeration device and a PID temperature control device, wherein the temperature sensor is placed in the sample chamber and connected to the PID temperature control device, and the refrigeration device is connected to the cooling module, The PID temperature control device is connected with the heating module.

Further, the refrigeration device is a low-temperature circulating bath, and the temperature sensor is a T-type thermocouple.

Furthermore, the inside of the cooling module has a U-shaped cooling groove, and the outer wall of the cooling module has two openings communicating with the U-shaped cooling groove, and the openings are connected with the low-temperature circulation bath.

The temperature control system provided by the utility model has the following advantages:

1) Simple structure, controllable volume, easy to integrate into other supporting systems;

2) The cooling module, sample chamber and heating module are all made of light-transmitting materials, so the specific process of chemical reaction and substance form change can be observed without customizing the light inlet.

Further, the temperature control system provided by the utility model has the following advantages:

1) The sample chamber has an input port and an output port, which can realize the purpose of dynamic sample addition;

2) The input port and output port of the sample chamber pass through the cooling module or heating module, which can make the structure of the temperature control system more compact;

3) Conductive glass is used as the heating module. Since the conductive glass is heated by a thin layer of metal oxide coated on the glass surface, the temperature of the entire glass surface is uniform, which can make the heating of the temperature control system more uniform;

4) The temperature sensor is placed in the sample chamber, which is conducive to more accurate measurement of the actual temperature of the sample, and the PID temperature control device uses the neural network PID algorithm to control the temperature, which is conducive to reducing the temperature of the temperature control system during the heating and cooling process error;

5) The use of a low-temperature circulating bath is beneficial to better control the temperature of the cooling module, and the T-type thermocouple measures the temperature quickly and accurately, which can make the temperature control system more accurately and truly reflect the actual temperature of the sample;

6) The U-shaped design of the cooling tank can increase the flow rate of the refrigerant in it, so that the cooling module can have a greater cooling rate.

Description of drawings

Fig. 1 is a schematic structural view of Embodiment 1 of the present utility model.

Fig. 2 is a schematic structural view of Embodiment 2 of the present utility model.

Detailed ways

In order to make the above purpose, features and advantages of the utility model more obvious and easy to understand, the specific implementation of the utility model will be described in detail below in conjunction with the accompanying drawings.

In the following description, a lot of specific details have been set forth in order to fully understand the utility model, but the utility model can also be implemented in other ways that are different from those described here, and those skilled in the art can do so without violating the connotation of the utility model. Under the circumstances, similar promotion is done, so the utility model is not limited by the specific embodiments disclosed below.

Example 1

Please refer to FIG. 1 , as shown in the figure, the cooling module 1 , the sample chamber 2 and the conductive glass 3 are stacked in sequence. Those skilled in the art can easily imagine that the above-mentioned cooling module can have multiple cooling modes such as water cooling and air cooling, and the material of the cooling module can be various light-transmitting materials such as polymethyl methacrylate, polycarbonate, polyparaphenylene, etc. One or more of ethylene glycol diformate, acrylonitrile-butadiene-styrene, the shape of the above-mentioned sample cavity can be rectangular, cylindrical or other suitable shapes, and the material of the sample cavity can be various transparent Optical materials such as one or more of polydimethylsiloxane, polyimide, polymethyl methacrylate, parylene, polytetrafluoroethylene, the above conductive glass can also be replaced by other transparent heating equipment. In this embodiment, the cooling module 1 is made of PMMA (polymethylmethacrylate), the sample chamber 2 is made of PDMS (polydimethylsiloxane), and the cooling module 1 has a U-shaped cooling groove inside 10, and the U-shaped cooling tank 10 is connected to the low-temperature circulating bath 9, the refrigerant in the low-temperature circulating bath 9 flows in from one side of the "U" and flows out from the other side of the "U", and the refrigerant flows smoothly in it, and the flow rate is relatively high. big. In addition, the heating layer on the surface of the conductive glass 3 can be separated into independent regions by an insulating tape (such as a part not coated with a thin layer of metal oxide or an insulating coating), and different voltages are connected to these different regions, which can be realized in a two-dimensional The temperature in the plane changes according to the gradient.

As shown in FIG. 1 , the sample chamber 2 has an input port 4 and output ports 5 and 6 . Those skilled in the art can easily see that as long as the sample chamber has one input port and one output port, dynamic sample addition can be realized. In specific implementation, the number of input ports and output ports can be set according to actual needs. In this embodiment, the two injection syringe pumps 11, 12 are connected in parallel with the mixer 13 through the conduit, the mixer 13 is connected with the input port 4 through the conduit, and the extraction syringe pump 14 is connected with the output port 5 through the conduit, wherein the mixer 12 can serve to mix the samples injected by the two injection syringe pumps 11.

As shown in Figure 1, the control module of the temperature control system includes a PID (proportional-integral-differential) temperature control device 7, a T-type thermocouple 8 and a low-temperature circulating bath 9. Those skilled in the art can easily think of other equipment that can be used for temperature control, such as a temperature controller, etc., equipment that can be used for temperature measurement, such as a thermometer, etc., and equipment that can be used for refrigeration, such as refrigerators, heat exchangers, etc. In this embodiment, the PID temperature control device 7 is connected to the conductive glass 3, and the heating value of the conductive glass 3 is controlled by the resistance value of the conductive glass itself and the power supply voltage value provided by the PID temperature control device 7 to the conductive glass 3 . And the T-type thermocouple 8 is placed in the sample chamber 2 through the output port 6 , and the PID temperature control device is connected with the T-type thermocouple 8 to detect the temperature in the sample chamber 2 .

This embodiment provides that the temperature control system realizes the temperature rise and fall of the sample chamber by the cooperative work of the cooling module and the heating module. Specifically, firstly, the temperature of the low-temperature circulating bath 9 is fixed so that the cooling module 1 provides a stable cooling capacity, and then through Control the heating value of the conductive glass 3 to control the heating or cooling of the sample chamber 2. At the same time, the PID temperature control device receives the temperature measured by the T-type thermocouple 8, and controls the working time of the conductive glass. When the resistance value of the conductive glass 3 itself and the power supply voltage value provided by the PID temperature control device 7 are within a certain range, the heating and cooling rate of the sample chamber 2 can be controlled.

Example 2

Please refer to Figure 2, as shown in the figure, the difference between Embodiment 2 and Embodiment 1 is that the input port 4 and the output port 5 of Embodiment 2 pass through the cooling module 1. Through this through design, the temperature control system is realized. External direct sample addition makes the structure of the temperature control system more compact. Those skilled in the art can easily imagine that the input port and the output port of the sample chamber of the present invention can be selected to pass through the cooling module or the heating module according to actual needs.

In order to better understand the utility model, the following will combine Example 1 of the utility model with a microscope, and according to the cell volume response, it is determined that the cells are added and removed during the cryoprotection process, under the conditions of different cooling temperatures and different cooling rates, Investigate the permeability parameters of the cell membrane. Wherein, the cryoprotectant is phosphate buffer containing cryoprotectant (CPA) or physiological saline containing cryoprotectant (CPA).

The specific implementation process in the process of adding cryoprotectant is as follows:

The cells used in the experiment are injected into the sample chamber 2 of the temperature control system through the injection syringe pump 11 . Since the cooling module and the heating module of the utility model are both transparent, the microscope can select the most suitable sample for observation in the entire sample cavity only by adjusting the position of the microscope stage. Generally, wait for fifteen minutes to make the cells adhere to the inner wall of the sample cavity 2 . Then, the injection pump 11 is loaded with a solution not containing a cryoprotectant, and the injection pump 12 is filled with a solution containing a cryoprotectant. Set the working speed of the injection syringe pump and the extraction syringe pump. The injection syringe pump 11 first injects the solution without cryoprotectant into the sample chamber 2 at a certain rate, and the extraction syringe pump 14 draws the solution outward at the same rate, and cools it at the same time. The module 1 and the conductive glass 3 work together, and the temperature of the solution in the sample chamber 2 is precisely controlled by the PID temperature control device through the temperature 8 feedback of the T-type thermocouple 8 . When the entire pipeline and the sample chamber 2 are filled with a solution that does not contain a cryoprotectant, turn off the injection syringe pump 11, start the injection syringe pump 12, and inject the solution containing cryoprotectant into the sample chamber 2 at the same working rate as the extraction syringe pump 14. If the solution of the cryoprotectant is used, the sample chamber completes the switching from the solution without the cryoprotectant to the solution containing the cryoprotectant, thereby realizing the process of simulating the addition of the cryoprotectant to the cells.

The difference between the process of simulating the removal of the cryoprotectant and the process of simulating the addition of the cryoprotectant is that the opening sequence of the injection syringe pump 11 and the injection syringe pump 12 is reversed.

Further, in order to better understand the utility model, the following uses the utility model to simulate the non-equilibrium freezing process and the rewarming and thawing process. Among them, the cryoprotectant solutions are all water-salt-cryoprotectant ternary solutions, and the components of the solutions are determined by the phase diagram of the multiple solution in the non-equilibrium freezing process.

The implementation process of simulating non-equilibrium freezing process is as follows:

The cells used in the experiment are injected into the sample chamber 2 of the temperature control system through the injection pump 11, the microscope is adjusted to find a suitable observation field, and the cells are attached to the inner wall of the sample chamber 2 after waiting for fifteen minutes. Next, fill the injection pump 11 with a low-concentration cryoprotectant solution, and fill the injection pump 12 with a high-concentration cryoprotectant solution. The injection syringe pump 11 and the extraction syringe pump 14 are started synchronously, and the flow rates of the two are controlled to be equal, so that the entire pipeline and the sample chamber 2 are filled with low-concentration cryoprotectant solution. At the same time, the cooling module 1 and the conductive glass 3 work together, and through the temperature feedback of the T-type thermocouple 8, the temperature of the solution in the sample chamber 2 is precisely controlled by the PID temperature control device to decrease according to the cooling rate of the actual freezing process. The next step is to turn on the injection pump 12, and by adjusting the working speed of the injection pump 11 and the injection pump 12, the switching of solutions containing different concentrations of cryoprotectant is realized, that is, the concentration of the solution in the sample chamber 2 changes according to the actual freezing process. Variety. The above is the specific operation of simulating the non-equilibrium freezing process of cells.

The difference between simulating rewarming and thawing process and simulating non-equilibrium freezing process is: reverse the opening sequence of injection syringe pump 11 and injection syringe pump 12, and precisely control the temperature of the solution in sample chamber 2 by the PID temperature control device according to the temperature rise of the actual thawing process rate increases.

Although the utility model is described in conjunction with the above embodiments, the utility model is not limited to the above embodiments, but is only limited by the appended claims, and those of ordinary skill in the art can easily modify and change it , but does not depart from the essential concept and scope of the present utility model.

Claims (9)

1. A temperature control system, comprising: a cooling module, a sample chamber, a heating module and a control module; wherein The cooling module, the sample chamber and the heating module are stacked sequentially, the control module collects the temperature of the sample chamber, and controls the temperature of the cooling module and the heating module; The cooling module, the sample chamber and the heating module all use light-transmitting materials. the 2. The temperature control system according to claim 1, wherein the sample chamber has at least one input port and at least one output port. the 3. The temperature control system according to claim 2, wherein the input port and the output port of the sample cavity pass through the cooling module or the heating module. the 4. The temperature control system according to claim 1, wherein the material of the cooling module is polymethyl methacrylate, polycarbonate, polyethylene terephthalate, acrylonitrile- One of butadiene-styrene. the 5. The temperature control system according to claim 1, wherein the material of the sample chamber is polydimethylsiloxane, polyimide, polymethyl methacrylate, parylene, poly One of tetrafluoroethylene. the 6. The temperature control system according to claim 1, wherein the material of the heating module is conductive glass. the 7. The temperature control system according to claim 1, wherein the control module comprises a temperature sensor, a refrigeration device and a PID temperature control device, wherein the temperature sensor is placed in the sample chamber and is controlled with the PID temperature The cooling device is connected to the cooling module, and the PID temperature control device is connected to the heating module. the 8. The temperature control system according to claim 7, wherein the refrigeration device is a low-temperature circulating bath, and the temperature sensor is a T-type thermocouple. the 9. The temperature control system according to claim 8, wherein the inside of the cooling module has a U-shaped cooling groove, and the outer wall of the cooling module has two openings communicating with the U-shaped cooling groove, the The opening is connected with the low temperature circulating bath. the

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