1. A liquid nitrogen evaporator for an X-ray single crystal diffractometer is characterized in that: the device comprises a conveying pipe which is arranged in a rectangular shape, wherein the inlet end of the conveying pipe is communicated with a flow valve;

a first heater is sleeved on one side of the conveying pipe, a second heater is sleeved on the other side of the conveying pipe, the lower portion of the first heater is communicated with a first flow limiting valve, the upper portion of the first heater is communicated with a second flow limiting valve, and the second flow limiting valve is communicated with an energy storage box;

the energy storage box is communicated with a flow stopping valve which is communicated with the upper part of the second heater, the lower part of the second heater is communicated with a flow stopping valve which is communicated with a pump assembly;

a first sensor positioned above the second heater is fixed in the conveying pipe, a second sensor positioned below the second heater is fixed in the conveying pipe, and an electromagnetic valve is arranged below the second sensor;

the outlet end of the conveying pipe is communicated with an air outlet valve.

2. The liquid nitrogen evaporator for an X-ray single crystal diffractometer according to claim 1, wherein: the energy storage box is communicated with a control valve, the control valve is communicated with auxiliary pipes which are spirally and uniformly distributed on the conveying pipe, and a third sensor is installed in the outlet end of the conveying pipe.

3. The liquid nitrogen evaporator for an X-ray single crystal diffractometer according to claim 2, wherein: the first heater comprises a first heat preservation layer and a first pipeline spirally arranged on the first heat preservation layer, the lower end of the first pipeline is communicated with the first flow limiting valve, and the upper end of the first pipeline is communicated with the second flow limiting valve.

4. The liquid nitrogen evaporator for an X-ray single crystal diffractometer according to claim 3, wherein: the second heater comprises a second heat-insulating layer and a second pipeline spirally arranged on the second heat-insulating layer, the upper end of the second pipeline is communicated with the flow stopping valve, and the lower end of the second pipeline is communicated with the flow stopping valve.

5. The liquid nitrogen evaporator for an X-ray single crystal diffractometer according to claim 4, wherein: the controller is electrically connected with the first flow limiting valve, the second flow limiting valve, the choke valve, the electromagnetic valve, the gas outlet valve, the flow valve, the control valve and the check valve.

6. The liquid nitrogen evaporator for an X-ray single crystal diffractometer according to claim 5, wherein: the method comprises the following evaporation methods:

s1: firstly, obtaining temperature information of a test sample needing to be reduced, and calculating liquid nitrogen amount, required nitrogen temperature and nitrogen amount according to the temperature information;

s2: the method comprises the steps that liquid nitrogen is conveyed to a flow valve through a liquid nitrogen tank, the controller obtains the amount of the liquid nitrogen, and based on judgment of the controller, when the required amount of the liquid nitrogen is reached, the controller is closed;

s3: the controller opens the first flow limiting valve and the second flow limiting valve, hot gas is input into the conveying pipe through the first flow limiting valve to carry out heat exchange evaporation on liquid nitrogen, the first sensor obtains the temperature A of the nitrogen in the conveying pipe, and based on the judgment of the controller, if the temperature A is inconsistent with the required temperature, the controller adjusts the flow of the hot gas passing through the first flow limiting valve and the second flow limiting valve until the temperature A is consistent with the required temperature of the nitrogen, and the controller opens the electromagnetic valve and the gas outlet valve;

s4: the second sensor acquires the temperature B of the nitrogen in the conveying pipe, and based on the judgment of the controller, if the temperature B is consistent with the required nitrogen temperature, the controller opens the electromagnetic valve and the gas outlet valve; if the temperature B is not consistent with the required nitrogen temperature, the controller opens the flow stopping valve, the flow blocking valve and the pump assembly, hot gas in the energy storage box is input into the second heater until the required nitrogen temperature is consistent, and the controller opens the electromagnetic valve;

s5: the third sensor acquires the temperature of outlet end nitrogen gas in the conveyer pipe, and based on the judgement of controller, if the nitrogen gas temperature of outlet end is unanimous with demand nitrogen gas temperature in the conveyer pipe, then open the air outlet valve, if the nitrogen gas temperature of outlet end is inconsistent with demand nitrogen gas temperature in the conveyer pipe, the controller opens the control valve, sends into steam and heaies up nitrogen gas in to the auxiliary pipe, until reaching demand temperature, opens the air outlet valve again.

Background

The X-ray diffractometer is a device for researching the crystal structure of a material, and the goniometer of the X-ray diffractometer is based on the Bragg diffractometer principle: the n lambda is designed as 2dsin theta, and the structure, the grain size, the crystallinity and the like of the material are detected by utilizing different angles of the surface rotation reflection line of the sample.

The conventional X-ray diffractometer usually detects in normal temperature air when testing a sample, and when low-temperature measurement is needed, the test sample needs to be cooled by liquid nitrogen, for example, Chinese patent publication numbers are as follows: CN 111678930 a. a detection device for measuring sample characteristics at low temperature by using an X-ray diffractometer, that is, liquid nitrogen is used to cool a test sample, but when liquid nitrogen is used, because it is in liquid state, it cannot be directly used, and only nitrogen gas is formed after gasification for reuse, but because the temperature of liquid nitrogen is extremely low, an ice-liquid mixture is formed during gasification, which is difficult to transmit to the X-ray diffractometer for use, and the liquid nitrogen needs to be heated up.

Therefore, a liquid nitrogen evaporator for an X-ray single crystal diffractometer is provided to adapt to the use of the X-ray single crystal diffractometer.

Disclosure of Invention

The invention aims to provide a liquid nitrogen evaporator for an X-ray single crystal diffractometer, which is suitable for the X-ray single crystal diffractometer and can control the temperature and the output quantity of nitrogen output.

In order to achieve the above object, the basic scheme of the invention is as follows: a liquid nitrogen evaporator for an X-ray single crystal diffractometer comprises a conveying pipe which is arranged in a rectangular shape, wherein the inlet end of the conveying pipe is communicated with a flow valve; a first heater is sleeved on one side of the conveying pipe, a second heater is sleeved on the other side of the conveying pipe, the lower portion of the first heater is communicated with a first flow limiting valve, the upper portion of the first heater is communicated with a second flow limiting valve, and the second flow limiting valve is communicated with an energy storage box; the energy storage box is communicated with a flow stopping valve which is communicated with the upper part of the second heater, the lower part of the second heater is communicated with a flow stopping valve which is communicated with a pump assembly; a first sensor positioned above the second heater is fixed in the conveying pipe, a second sensor positioned below the second heater is fixed in the conveying pipe, and an electromagnetic valve is arranged below the second sensor; the outlet end of the conveying pipe is communicated with an air outlet valve.

Furthermore, the energy storage box is communicated with a control valve, the control valve is communicated with auxiliary pipes which are spirally and uniformly distributed on the conveying pipe, and a third sensor is installed in the outlet end of the conveying pipe.

Has the advantages that: in this scheme, utilize the nitrogen gas temperature of third sensor detection conveyer pipe exit end, if the nitrogen gas temperature that the temperature still did not reach the demand, then the choke valve can be controlled to the controller and open to the intraductal input steam of auxiliary pipe, utilize steam to heat up nitrogen gas, reach the nitrogen gas temperature of demand, reach the demand temperature at last and open the air outlet valve again.

Further, the first heater comprises a first heat preservation layer and a first pipeline spirally arranged on the first heat preservation layer, the lower end of the first pipeline is communicated with the first flow limiting valve, and the upper end of the first pipeline is communicated with the second flow limiting valve.

Has the advantages that: in this scheme, the first pipeline that the spiral was arranged carries out the hot exchange time with extension steam and liquid nitrogen, reaches the purpose that carries out abundant evaporation intensification to the liquid nitrogen, and the heat preservation keeps warm to the steam in the first pipeline, reduces the heat energy loss volume of steam.

Further, the second heater includes the second heat preservation and is the second pipeline of spiral arrangement on the second heat preservation, and the upper end and the flow stopping valve intercommunication of second pipeline, the lower extreme and the choke valve intercommunication of second pipeline.

Has the advantages that: in this scheme, when the steam in the energy storage case heaied up nitrogen gas through the second pipeline, the time of the second pipeline extension steam of spiral arrangement and nitrogen gas heat exchange, the heat preservation keeps warm to the steam in the second pipeline.

The controller is electrically connected with the first flow limiting valve, the second flow limiting valve, the choke valve, the electromagnetic valve, the gas outlet valve, the flow valve, the control valve and the check valve.

Has the advantages that: based on the information of the first sensor, the second sensor and the third sensor, the first flow limiting valve, the second flow limiting valve, the flow blocking valve, the electromagnetic valve, the gas outlet valve, the flow valve, the control valve and the flow stopping valve are controlled, the purpose of intelligently evaporating liquid nitrogen is achieved, and the temperature of nitrogen can be fully controlled.

Further, the method comprises the following evaporation methods:

s1: firstly, obtaining temperature information of a test sample needing to be reduced, and calculating liquid nitrogen amount, required nitrogen temperature and nitrogen amount according to the temperature information;

s2: the method comprises the steps that liquid nitrogen is conveyed to a flow valve through a liquid nitrogen tank, the controller obtains the amount of the liquid nitrogen, and based on judgment of the controller, when the required amount of the liquid nitrogen is reached, the controller is closed;

s3: the controller opens the first flow limiting valve and the second flow limiting valve, hot gas is input into the conveying pipe through the first flow limiting valve to carry out heat exchange evaporation on liquid nitrogen, the first sensor obtains the temperature A of the nitrogen in the conveying pipe, and based on the judgment of the controller, if the temperature A is inconsistent with the required temperature, the controller adjusts the flow of the hot gas passing through the first flow limiting valve and the second flow limiting valve until the temperature A is consistent with the required temperature of the nitrogen, and the controller opens the electromagnetic valve and the gas outlet valve;

s4: the second sensor acquires the temperature B of the nitrogen in the conveying pipe, and based on the judgment of the controller, if the temperature B is consistent with the required nitrogen temperature, the controller opens the electromagnetic valve and the gas outlet valve; if the temperature B is not consistent with the required nitrogen temperature, the controller opens the flow stopping valve, the flow blocking valve and the pump assembly, hot gas in the energy storage box is input into the second heater until the required nitrogen temperature is consistent, and the controller opens the electromagnetic valve;

s5: the third sensor acquires the temperature of outlet end nitrogen gas in the conveyer pipe, and based on the judgement of controller, if the nitrogen gas temperature of outlet end is unanimous with demand nitrogen gas temperature in the conveyer pipe, then open the air outlet valve, if the nitrogen gas temperature of outlet end is inconsistent with demand nitrogen gas temperature in the conveyer pipe, the controller opens the control valve, sends into steam and heaies up nitrogen gas in to the auxiliary pipe, until reaching demand temperature, opens the air outlet valve again.

Has the advantages that: in this scheme, through first sensor, second sensor and third sensor to and the cooperation of controller and first restriction valve, second restriction valve, choke valve, solenoid valve, play air valve, flow valve, control valve and check valve, reach the purpose of multistage intensification, guarantee the output temperature of nitrogen gas, be adapted to the demand of X ray single crystal diffractometer.

The principle and the beneficial effects of the invention are as follows: (1) utilize first heater, second heater and auxiliary tube to carry out tertiary cooperation in this scheme, reach and evaporate the liquid nitrogen to the purpose of temperature control is carried out to the temperature of regulation and control nitrogen gas output.

(2) In this scheme, through the cooperation of first restriction valve, second restriction valve, choke valve, solenoid valve, play air valve, flow valve, control valve and check valve, guaranteed the accurate nature of the temperature control of nitrogen gas with, be adapted to the demand of X ray single crystal diffractometer to nitrogen gas.

Of course, the application does not necessarily require that all of the above-described technical effects be achieved at the same time.

Drawings

FIG. 1 is an isometric view of a liquid nitrogen vaporizer for use in an X-ray single crystal diffractometer in an embodiment of the present invention;

FIG. 2 is a sectional view of a liquid nitrogen vaporizer used in an X-ray single crystal diffractometer according to an embodiment of the present invention;

FIG. 3 is a circuit control diagram of a liquid nitrogen evaporator for an X-ray single crystal diffractometer according to an embodiment of the present invention.

Detailed Description

In the following, the technical solutions in the embodiments of the present invention will be clearly and completely described with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments.

In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, are merely for convenience in describing the present invention and simplifying the description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention.

Reference numerals in the drawings of the specification include: the device comprises a second heater 11, a second pipeline 111, a delivery pipe 12, a first heater 13, a first pipeline 131, a flow valve 14, an output pipe 15, a check valve 21, a second check valve 22, a first check valve 23, a control valve 25, an air outlet valve 26, an electromagnetic valve 27, a check valve 28, an air suction pump 29, a first sensor 31, a second sensor 32 and a third sensor 33.

Example (b):

substantially as shown in figures 1, 2 and 3: the utility model provides a liquid nitrogen evaporator for X ray single crystal diffractometer, is including being the conveyer pipe 12 that the rectangle was arranged, and the entrance point intercommunication of conveyer pipe 12 has flow valve 14, and one side cover of conveyer pipe 12 is equipped with first heater 13, and the opposite side cover of conveyer pipe 12 is equipped with second heater 11, and the exit end of conveyer pipe 12 seals, and the exit end intercommunication of conveyer pipe 12 has output tube 15, and the intercommunication has air outlet valve 26 on the output tube 15.

In this embodiment, the first heater 13 includes a first heat-insulating layer and a first pipeline 131 spirally arranged on the first heat-insulating layer, a first flow limiting valve 23 is communicated with the lower end of the first pipeline 131, a second flow limiting valve 22 is communicated with the upper end of the first pipeline 131, and an energy storage tank is communicated with the second flow limiting valve 22. The second heater 11 comprises a second insulating layer and a second pipeline 111 spirally arranged on the second insulating layer, the upper end of the second pipeline 111 is communicated with a flow stopping valve 21 communicated with the energy storage tank, the lower end of the second pipeline 111 is communicated with a flow blocking valve 28, the flow blocking valve 28 is communicated with an air suction pump 29, and the air suction pump 29 is communicated with an exhaust gas tank (not shown in the figure).

The energy storage tank is connected with a choke valve 28, and the choke valve 28 is connected with an auxiliary pipe spirally arranged at the outlet end of the conveying pipe 12, and the auxiliary pipe is communicated with the exhaust gas tank.

In this embodiment, a first sensor 31 located above the second heater 11 is installed in the delivery pipe 12, a second sensor 32 located below the second heater 11 is installed in the delivery pipe 12, an electromagnetic valve 27 installed on the delivery pipe 12 is disposed below the second sensor 32, and a third sensor 33 is installed at the outlet end of the delivery pipe 12.

The embodiment also comprises a controller, wherein the first sensor 31, the second sensor 32 and the third sensor 33 are all electrically connected with the controller, and the first flow limiting valve 23, the second flow limiting valve 22, the choke valve 28, the electromagnetic valve 27, the gas outlet valve 26, the flow valve 14, the control valve 25 and the check valve 21 are all electrically connected with the controller. In the present embodiment, the first sensor 31, the second sensor 32, and the third sensor 33 are all temperature sensors.

In this embodiment, the liquid nitrogen evaporation method includes the following steps:

s1: the temperature information of the test sample needing to be reduced is obtained firstly, and the liquid nitrogen amount, the required nitrogen temperature and the nitrogen amount are calculated through the temperature information. For example: the temperature of the test sample is initially measured, the quantity a to be released at the temperature 10 ℃ which needs to be lowered by the test sample is calculated by using the formula Q ═ C × m × Δ t, (Q release represents the quantity of heat released, C represents the specific heat capacity of the substance, m represents the mass of the substance, and Δ t represents the amount of change in temperature), and the quantity a to be released, the temperature rise of nitrogen again 10 ℃ and the initial temperature of nitrogen are substituted into the formula: calculating the mass of nitrogen gas by using the formula: v2 ═ 647 × V1 (amount of nitrogen at V1, V2, and 1L of nitrogen ═ 647L) determined the amount of liquid nitrogen.

S2: liquid nitrogen is conveyed to the flow valve 14 through the liquid nitrogen tank, the controller controls the opening and closing of the flow valve 14, and when the nitrogen amount reaches the required amount, the controller closes the flow valve 14.

S3: the controller opens first restriction valve 23 and second restriction valve 22, and input steam through first restriction valve 23 in to conveyer pipe 12 and heat the liquid nitrogen, so that the liquid nitrogen evaporates, first sensor 31 acquires the temperature A of nitrogen gas in conveyer pipe 12, based on the judgement of controller, if temperature A is inconsistent with the demand temperature (the temperature is low, reach the intensification purpose), the controller adjusts the aperture through first restriction valve 23 and second restriction valve 22, with the volume of control steam in first pipeline 131, guarantee the heat transfer effect, until the temperature of nitrogen gas is unanimous with the nitrogen gas temperature of demand, then the controller directly opens solenoid valve 27 and goes out gas valve 26.

S4: the second sensor 32 obtains the temperature B of nitrogen gas in the conveyer pipe 12, based on the judgement of controller, if temperature B is unanimous with demand nitrogen gas temperature, solenoid valve 27 is opened to the controller, nitrogen gas flow direction conveyer pipe 12's exit end, if the third sensor 33 obtains nitrogen gas temperature in the conveyer pipe 12 and temperature B nonconformity (the temperature is crossed lowly, does not reach the intensification requirement), the controller opens flow stopping valve 21, choke valve 28 and aspiration pump 29, to the interior steam of the input energy storage incasement of second heater 11, until reaching the nitrogen gas temperature of demand, solenoid valve 27 and air outlet valve 26 are opened to the controller.

S5: the third sensor 33 acquires the temperature of outlet end nitrogen gas in the conveyer pipe 12 to with information transmission to controller, based on the judgement of controller, if the nitrogen gas temperature of outlet end is inconsistent with demand nitrogen gas temperature in the conveyer pipe 12, control valve 25 is opened to the controller, and the energy storage case is to the intraductal input steam of auxiliary pipe in order to heat up nitrogen gas, until reaching demand nitrogen gas temperature, the controller opens air outlet valve 26.

Of course, in this embodiment, the controller can also control the opening of the gas outlet valve 26 to control the gas outlet amount of the nitrogen gas, so as to adapt to the temperature requirement of the X-ray single crystal diffractometer on the nitrogen gas. This scheme is arranged with the form of pipeline, can integrate and arrange, is applicable to in less space, does benefit to X ray single crystal diffractometer and uses nitrogen gas. Simultaneously, this embodiment stores steam with the energy storage case, utilizes waste heat, reaches energy-conserving purpose.

The foregoing is merely an example of the present invention and common general knowledge in the art of specific structures and/or features of the invention has not been set forth herein in any way. It should be noted that, for those skilled in the art, without departing from the structure of the present invention, several changes and modifications can be made, which should also be regarded as the protection scope of the present invention, and these will not affect the effect of the implementation of the present invention and the practicability of the patent. The scope of the claims of the present application shall be determined by the contents of the claims, and the description of the embodiments and the like in the specification shall be used to explain the contents of the claims.