US20220111304A1 - Automatic tritium extraction method for environmental monitoring - Google Patents

Automatic tritium extraction method for environmental monitoring Download PDF

Info

Publication number
US20220111304A1
US20220111304A1 US17/523,486 US202117523486A US2022111304A1 US 20220111304 A1 US20220111304 A1 US 20220111304A1 US 202117523486 A US202117523486 A US 202117523486A US 2022111304 A1 US2022111304 A1 US 2022111304A1
Authority
US
United States
Prior art keywords
distillation
pump
distillation chamber
chamber
started
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US17/523,486
Inventor
Zhidong Pan
Shibo LIU
Naizheng Zhou
Cheng Wu
Lulu Zheng
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang Hengda Instrumentation Co Ltd
Original Assignee
Zhejiang Hengda Instrumentation Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from CN201910496784.4A external-priority patent/CN110180199B/en
Application filed by Zhejiang Hengda Instrumentation Co Ltd filed Critical Zhejiang Hengda Instrumentation Co Ltd
Priority to US17/523,486 priority Critical patent/US20220111304A1/en
Publication of US20220111304A1 publication Critical patent/US20220111304A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/42Regulation; Control
    • B01D3/4211Regulation; Control of columns
    • B01D3/4294Feed stream
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/02Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in boilers or stills
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/143Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
    • B01D3/146Multiple effect distillation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/32Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/42Regulation; Control
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/34Purifying; Cleaning
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • G01N1/4022Concentrating samples by thermal techniques; Phase changes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/0011Heating features
    • B01D1/0017Use of electrical or wave energy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/006Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • G01N1/4022Concentrating samples by thermal techniques; Phase changes
    • G01N2001/4033Concentrating samples by thermal techniques; Phase changes sample concentrated on a cold spot, e.g. condensation or distillation

Definitions

  • the invention belongs to the technical fields of environmental protection and automatic equipment, in particular to an automatic tritium extraction device and method for environmental monitoring.
  • Tritium is a radioactive substance with a half-life period of 12.6 years. Most tritium in the air will eventually turn into tritium oxide-water steam which, together with ordinary water, is involved in water circulation, and thus, human beings are likely to be exposed to tritium radiation. During environmental protection, monitoring of the content of tritium in water and air has received extensive international attention.
  • the technical issue to be settled by the invention is to overcome the defects of the prior art by providing an automatic tritium extraction device and method for environmental monitoring to fulfill automatic distillation of tritium samples and automatic cleaning of distillation chambers and to save labor costs.
  • an automatic tritium extraction device for environmental monitoring comprises a distillation chamber, a temperature control unit used to heat the distillation chamber, a condensation unit connected to the distillation chamber through a delivery pipe, and an auxiliary condensation unit used to cyclically deliver a condensing agent into the condensation unit, wherein the distillation chamber is connected to a first pump for delivering agents into the distillation chamber, a second pump for delivering samples into the distillation chamber, and a third pump for communicating the distillation chamber with the outside; and the delivery pipe comprises a first vertical pipe connected to the top of the distillation chamber, a second vertical pipe connected to the top of the condensation unit, and an oblique pipe obliquely connected between the first pipe and the second pipe, and the oblique pipe inclines upwards from the distillation chamber to the condensation unit.
  • first spherical bulge with a larger inner diameter is disposed on the first vertical pipe
  • second spherical bulge with a large inner diameter is disposed on the second vertical pipe.
  • the first pump is connected to an upper part of the distillation chamber
  • the second pump is also connected to the upper part of the distillation chamber
  • the third pump is connected to the bottom of the distillation chamber and is used to deliver air into the distillation chamber or discharge samples in the distillation chamber to the outside.
  • a main part of the distillation chamber is cylindrical
  • the bottom of the distillation chamber is conical
  • the temperature control unit comprises heating elements encircling the outer wall of the main part of the distillation chamber and a temperature control switch disposed between the heating elements and the outer wall of the distillation chamber.
  • the agents include a cleaning agent and a distilling agent.
  • the condensation unit comprises a condensing agent circulation chamber and a spiral heat-exchange tube disposed in the condensing agent circulation chamber, and the condensing agent circulation chamber comprises an inlet connected to the second vertical pipe and an outlet connected to a collection tank.
  • the second pump is connected to a sample tank for containing the samples.
  • the auxiliary condensation unit comprises a cavity for storing the condensing agent, a power device for cyclically delivering the condensing agent into the condensing agent circulation chamber, an upper tube connected to an upper part of the condensing agent circulation chamber, and a lower tube connected to a lower part of the condensing agent circulation chamber.
  • the invention further discloses an automatic tritium extraction method for environmental monitoring, which comprises the following steps:
  • a cleaning agent is used, a first pump is started to pump a specified quantity of the cleaning agent into the distillation chamber, a temperature control unit is started to heat the distillation chamber to a preset temperature, then a third pump is started to deliver outside air into the distillation chamber, and when agitation cleaning of the distillation chamber is completed, mixed liquor in the distillation chamber is discharged by the third pump;
  • a distilling agent is used, a second pump is started to pump a specified quantity of samples into the distillation chamber, then, the first pump is started to pump a specified quantity of the distilling agent into the distillation chamber, and the temperature control unit is started to maintain the temperature of the outer wall of the distillation chamber at the preset temperature, and a collection tank containing finished products is replaced with an empty collection tank;
  • the distilling agent is used, the second pump further pumps a specified quantity of samples into the distillation chamber, the first pump is started to pump a specified quantity of the distilling agent into the distillation chamber, and the temperature control unit is started to maintain the distillation chamber at a preset temperature and is stopped when the distillation amount reaches a preset value;
  • Step 2) and Step 3 Carrying out condensation when Step 2) and Step 3) are performed: an auxiliary condensation unit is started, and a condensing agent is delivered into a condensing agent circulation chamber via a lower tube and flows back into a cavity via an upper tube after being subjected to heat exchange in the condensing agent circulation chamber;
  • the second pump further pumps the rest of samples in a sample tank into the distillation chamber, and the third pump is started to discharge all the samples out of the distillation chamber.
  • the preset temperature in Step 1) and Step 2) is 80-100° C.
  • the preset value in Step 3) is 500-700 mL.
  • the invention has the following beneficial effects: fully-automatic distillation and condensation of environmental tritium samples, automatic cleaning of the distillation chamber, and automatic and accurate addition of required agents are realized.
  • the automatic tritium extraction device fills the blank of fully-automatic distillation and purification of environmental tritium analysis and can complete fully-automatic acquisition, preparation, distillation, purification, measurement and analysis of environmental tritium together with a tritium analysis meter, so that an environmental tritium analysis system is free of attendance in the entire process, and fully-automatic monitoring of regions with severe environmental tritium radiation is realized; and the automatic tritium extraction device greatly reduces manual intervention, so that monitoring results are more accurate, labor costs are saved, and the probability of physical harm to relevant service personnel is drastically lowered.
  • FIG. 1 is a flow structural diagram of the invention.
  • FIG. 2 is a collaboration diagram of a temperature control unit and a distillation chamber of the invention.
  • an automatic tritium extraction device for environmental monitoring comprises a distillation chamber 1 , a temperature control unit 2 , a condensation unit 4 and an auxiliary condensation unit 5 , wherein a main part of the distillation chamber 1 is cylindrical, and the bottom of the distillation chamber 1 is conical; the temperature control unit 2 encircles one part of the outer wall of the main part of the distillation chamber 1 and is used to heat the distillation chamber 1 ; one end of the condensation unit 4 is connected to the top of the distillation chamber 1 , and the other end of the condensation unit 4 is connected to a delivery pipe 3 at the top of the condensation unit 4 ; and the auxiliary condensation unit 5 is connected to the condensation unit 4 and is used to cyclically deliver a condensing agent into the condensation unit 4 .
  • An upper part of the distillation chamber 1 is connected to multiple agent bottles through multiple pipes and a first pump 11 , wherein cleaning agents or distilling agents are contained in the multiple bottles 15 , and the first pump 11 may be a WK10 high-precision micro peristaltic pump capable of accurately regulating and controlling the delivery quantity.
  • the upper part of the distillation chamber 1 is also connected to a sample tank 7 containing to-be-tested tritium-containing samples through a pipe and a second pump 12 , wherein the second pump 12 is used to transport the tritium-containing samples into the distillation chamber 1 .
  • a sample outlet 14 is formed in the conical bottom of the distillation chamber 1 and is communicated with the outside through a third pump 13 to discharge the samples in the distillation chamber 1 to the outside.
  • the temperature control unit 2 comprises heating elements 21 encircling the outer wall of the main part of the distillation chamber 1 and a temperature control switch 22 disposed between the heating elements 21 and the outer wall of the distillation chamber 1 , wherein the heating elements 21 generate heat for distillation in the distillation chamber 1 ; and the temperature control switch 22 is used to sense the temperature of the outer wall surface of the distillation chamber 1 in real time, timely and automatically power on the heating elements 21 to heat the distillation chamber 1 when the temperature of the outer wall surface of the distillation chamber 1 is lower than a preset value 80-100° C., and timely and automatically power off the heating elements 21 , when the temperature of the outer wall surface of the distillation chamber 1 is higher than the preset value 80-100° C., to maintain the temperature of the distillation chamber 1 at the preset value to ensure continuous and efficient distillation.
  • the condensation unit 4 comprises a hollow condensing agent circulation chamber 41 and a spiral heat-exchange tube 42 disposed in the condensing agent circulation chamber 41 , wherein the spiral heat-exchange tube 42 allows tritium sample steam to circulate therein, the condensing agent circulation chamber 41 is filled with the condensing agent which may be deionized distilled water, the tritium sample steam in the spiral heat-exchange tube 42 is cooled and condensed into liquid by the condensing agent, an inlet 411 communicated with the delivery pipe 3 is formed in the top of the condensing agent circulation chamber 41 , an outlet 412 communicated with an environmental tritium sample collection tank 6 may be formed in the bottom of the condensing agent circulation chamber 41 , and an airtight container is formed by other parts of the condensing agent circulation chamber 41 to allow the condensing agent to circulate therein.
  • the condensing agent circulation chamber 41 is filled with the condensing agent which may be deionized distilled water
  • the auxiliary condensation unit 5 is used to control the condensing process of the condensation unit 4 and comprises a cavity 51 for storing the condensing agent, an upper tube 52 for communicating the cavity 51 with an upper part of the condensing agent circulation chamber 41 , a lower tube 53 for communicating the cavity 51 with a lower part of the condensing agent circulation chamber 41 , and a power device for driving the condensing agent to flow into the condensing agent circulation chamber 41 from the cavity 51 through the lower tube 53 or driving the condensing agent to flow into the cavity 51 from the condensing agent circulation chamber 41 through the upper tube 52 , wherein the power device is a peristaltic pump or a diaphragm pump and is used to drive the condensing agent to cyclically flow between the condensing agent circulation chamber 41 and the cavity 51 .
  • the power device is a peristaltic pump or a diaphragm pump and is used to drive the condensing agent to cyclically flow between the condensing agent circulation
  • the delivery pipe 3 for guiding distillation gas generated in the distillation chamber 1 into the condensation unit 4 comprises a first vertical pipe 31 connected to the top of the distillation chamber 1 , a second vertical pipe 32 connected to the top of the condensing agent circulation chamber 41 , and an oblique pipe 33 obliquely connected between the first vertical pipe 31 and the second vertical pipe 32 , wherein the top of the distillation chamber 1 is located on the same horizontal plane as the top of the condensing agent circulation chamber 41 , and the oblique pipe 33 inclines upwards from the distillation chamber 1 to the condensation unit 4 , that is, the second vertical pipe 32 is longer than the first vertical pipe 31 .
  • a first spherical bulge 311 with a larger inner diameter is formed in the first vertical pipe 31 , is close to the top of the distillation chamber 1 and is spaced from the top of the top of the distillation chamber 1 by a small distance, so that steam output from the top of the distillation chamber 1 passes through the first vertical pipe 31 with the inner diameter sharply decreased to form a micro positive pressure and then enters the first spherical bulge 311 with the larger inner diameter to form a micro negative pressure, in this way, sample drops carried by steam are prevented from entering the condensation unit 4 via the delivery pipe 3 , and the monitoring accuracy of the environmental tritium samples is guaranteed.
  • a second spherical bulge 321 with a larger inner diameter is formed in the second vertical pipe 32 , is close to the top of the condensing agent circulation chamber 41 and is spaced from the top of the condensing agent circulation chamber 41 by a small distance, so that steam entering the condensing agent circulation chamber 41 first passes through the second spherical bulge 321 with the inner diameter sharply increased to be pre-condensed and then enters the condensing agent circulation chamber 41 via the second vertical pipe 32 with a smaller inner diameter, thus improving the condensation efficiency.
  • the distillation chamber 1 is automatically cleaned at first, then, the environmental tritium samples and the distilling agent enter the distillation chamber, the temperature control unit 2 is started to carry out controllable distillation, and steam enters the steam delivery pipe 3 , wherein one part of the steam is condensed to flow back into the distillation chamber 1 to be re-distillated under the effect of the structure of the first spherical bulge 311 at a port of the first vertical pipe 31 and the oblique upward structure of the oblique pipe 33 , and the other part of the steam enters the condensation unit 4 via the steam delivery pipe 3 and is mostly condensed in the spiral heat-exchange tube 42 in the condensing agent circulation chamber 41 under the effect of the structure and temperature to flow into the environmental tritium sample collection tank 6 under the effect of gravity; and the steam and the condensing agent exchange heat in the spiral heat-exchange tube 42 , so that the temperature of the steam drops, the temperature of the condensing agent rise
  • An automatic tritium extraction method for environmental monitoring comprises the following steps:
  • a cleaning agent is used, a first pump is started to pump the cleaning agent into the distillation chamber, and the quantity of the cleaning agent pumped into the distillation chamber is accurately controlled; the temperature control unit is started to increase the temperature of the outer wall surface of the distillation chamber 1 to 80-100° C.; a third pump is started to deliver outside air into the distillation chamber 1 to agitate the cleaning agent to clean the distillation chamber 1 , and at this moment, a second pump and a condensation unit are stopped; and when agitation cleaning of the distillation chamber is completed a period of time later, the third pump is started again to discharge mixed liquor in the distillation chamber 1 out of the distillation chamber 1 via a sample outlet 14 ;
  • a collection tank containing environmental tritium finished products in step 2) is replaced with an empty collection tank, and the second pump further pumps one third of samples into the distillation chamber 1 from the sample tank 7 ;
  • the first pump is started to pump a specified quantity of the distilling agent, in proportion with the one third of samples, into the distillation chamber 1 from different bottles; and temperature control unit is kept in the on-state to maintain the temperature of the outer wall surface of the distillation chamber 1 at 80-100° C. and is stopped when the distillation amount reaches a preset value 500-700 mL;
  • Step 2) and Step 3 Carrying out condensation when Step 2) and Step 3) are performed: an auxiliary condensation unit is started, a power device delivers a condensing agent into a condensing agent circulation chamber 41 from a cavity via a lower tube 53 and recovers the condensing agent subjected to heat exchange in the condensing agent circulation chamber 41 back into the cavity 51 via an upper tube in the direction of arrow;
  • the second pump further pumps the last one third of samples into the distillation chamber 1 from the sample tank 7 ; and the first pump is stopped, and the third pump is started to discharge all the samples 1 in the distillation chamber 1 out of the distillation chamber 1 via the sample outlet 14 ; and

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Engineering & Computer Science (AREA)
  • Biomedical Technology (AREA)
  • Molecular Biology (AREA)
  • Sampling And Sample Adjustment (AREA)
  • Measurement Of Radiation (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

An automatic tritium extraction method for environmental monitoring comprises the following steps: 1) cleaning of a distillation chamber; 2) distillation rising; 3) distillation; 4) condensation; 5) discharging samples out of the distillation chamber. By the adoption of the automatic tritium extraction device and method for environmental monitoring, fully-automatic distillation and condensation of environmental tritium samples, automatic cleaning of the distillation chamber, and automatic and accurate addition of required agents are realized, and fully-automatic acquisition, preparation, distillation, purification, measurement and analysis of environmental tritium can be completed; and manual intervention is reduced, so that monitoring results are more accurate, and labor costs are saved.

Description

    CROSS REFERENCE TO RELATED APPLICATIONS
  • This application is a Divisional of co-pending application Ser. No. 16/896,689, filed on Jun. 9, 2020, for which priority is claimed under 35 U.S.C. § 120; and this application claims priority of Application No. 201910496784.4 filed in China on Jun. 10, 2019 under 35 U.S.C. § 119; the entire contents of all of which are hereby incorporated by reference.
  • BACKGROUND OF THE INVENTION 1. Technical Field
  • The invention belongs to the technical fields of environmental protection and automatic equipment, in particular to an automatic tritium extraction device and method for environmental monitoring.
  • 2. Description of Related Art
  • Tritium is a radioactive substance with a half-life period of 12.6 years. Most tritium in the air will eventually turn into tritium oxide-water steam which, together with ordinary water, is involved in water circulation, and thus, human beings are likely to be exposed to tritium radiation. During environmental protection, monitoring of the content of tritium in water and air has received extensive international attention. Of all existing tritium monitoring methods, indirect measurement methods are obviously superior to other methods and are implemented on the basis of the following principle: air tritium oxide samples are prepared through an air condensation method and are taken back to the laboratory, then tritium sample purification is carried out through a manual distillation and condensation method, after that, the tritium oxide samples and a scintillation solution are quantitatively injected into sample bottles in a certain proportion, and finally, the sample bottles are placed into an instrument one by one for analysis. Existing distillation and concentration methods typically include semi-automatic distillation and manual distillation, wherein semi-automatic distillation can fulfill automatic distillation of single samples, and cleaning is performed manually after distillation; and traditionally, manual distillation is carried out in the laboratory, and all operations are performed manually. Both distillation methods have the following drawbacks: 1, sample preparation personnel may be exposed to radiation when the concentration of tritium samples is high; 2, experimenters should be highly skilled to complete quantitative sample preparation, personal operation errors may be caused, the experimental operation time is long, and manual attendance is required; and 4, the cleaning process needs to be manually completed, so that full automation of the process is not available, and online monitoring of air tritium cannot be realized either.
  • BRIEF SUMMARY OF THE INVENTION
  • The technical issue to be settled by the invention is to overcome the defects of the prior art by providing an automatic tritium extraction device and method for environmental monitoring to fulfill automatic distillation of tritium samples and automatic cleaning of distillation chambers and to save labor costs.
  • The technical solution adopted by the invention to settle the aforesaid technical issue is as follows: an automatic tritium extraction device for environmental monitoring comprises a distillation chamber, a temperature control unit used to heat the distillation chamber, a condensation unit connected to the distillation chamber through a delivery pipe, and an auxiliary condensation unit used to cyclically deliver a condensing agent into the condensation unit, wherein the distillation chamber is connected to a first pump for delivering agents into the distillation chamber, a second pump for delivering samples into the distillation chamber, and a third pump for communicating the distillation chamber with the outside; and the delivery pipe comprises a first vertical pipe connected to the top of the distillation chamber, a second vertical pipe connected to the top of the condensation unit, and an oblique pipe obliquely connected between the first pipe and the second pipe, and the oblique pipe inclines upwards from the distillation chamber to the condensation unit.
  • Furthermore, a first spherical bulge with a larger inner diameter is disposed on the first vertical pipe, and a second spherical bulge with a large inner diameter is disposed on the second vertical pipe.
  • Furthermore, the first pump is connected to an upper part of the distillation chamber, the second pump is also connected to the upper part of the distillation chamber, and the third pump is connected to the bottom of the distillation chamber and is used to deliver air into the distillation chamber or discharge samples in the distillation chamber to the outside.
  • Furthermore, a main part of the distillation chamber is cylindrical, the bottom of the distillation chamber is conical, and the temperature control unit comprises heating elements encircling the outer wall of the main part of the distillation chamber and a temperature control switch disposed between the heating elements and the outer wall of the distillation chamber.
  • Furthermore, the agents include a cleaning agent and a distilling agent.
  • Furthermore, the condensation unit comprises a condensing agent circulation chamber and a spiral heat-exchange tube disposed in the condensing agent circulation chamber, and the condensing agent circulation chamber comprises an inlet connected to the second vertical pipe and an outlet connected to a collection tank.
  • Furthermore, the second pump is connected to a sample tank for containing the samples.
  • Furthermore, the auxiliary condensation unit comprises a cavity for storing the condensing agent, a power device for cyclically delivering the condensing agent into the condensing agent circulation chamber, an upper tube connected to an upper part of the condensing agent circulation chamber, and a lower tube connected to a lower part of the condensing agent circulation chamber.
  • The invention further discloses an automatic tritium extraction method for environmental monitoring, which comprises the following steps:
  • 1) Cleaning of a distillation chamber: a cleaning agent is used, a first pump is started to pump a specified quantity of the cleaning agent into the distillation chamber, a temperature control unit is started to heat the distillation chamber to a preset temperature, then a third pump is started to deliver outside air into the distillation chamber, and when agitation cleaning of the distillation chamber is completed, mixed liquor in the distillation chamber is discharged by the third pump;
  • 2) Distillation rinsing: a distilling agent is used, a second pump is started to pump a specified quantity of samples into the distillation chamber, then, the first pump is started to pump a specified quantity of the distilling agent into the distillation chamber, and the temperature control unit is started to maintain the temperature of the outer wall of the distillation chamber at the preset temperature, and a collection tank containing finished products is replaced with an empty collection tank;
  • 3) Distillation: the distilling agent is used, the second pump further pumps a specified quantity of samples into the distillation chamber, the first pump is started to pump a specified quantity of the distilling agent into the distillation chamber, and the temperature control unit is started to maintain the distillation chamber at a preset temperature and is stopped when the distillation amount reaches a preset value;
  • 4) Carrying out condensation when Step 2) and Step 3) are performed: an auxiliary condensation unit is started, and a condensing agent is delivered into a condensing agent circulation chamber via a lower tube and flows back into a cavity via an upper tube after being subjected to heat exchange in the condensing agent circulation chamber;
  • 5) Discharging samples out of the distillation chamber: the second pump further pumps the rest of samples in a sample tank into the distillation chamber, and the third pump is started to discharge all the samples out of the distillation chamber.
  • Preferably, the preset temperature in Step 1) and Step 2) is 80-100° C., and the preset value in Step 3) is 500-700 mL.
  • The invention has the following beneficial effects: fully-automatic distillation and condensation of environmental tritium samples, automatic cleaning of the distillation chamber, and automatic and accurate addition of required agents are realized. The automatic tritium extraction device fills the blank of fully-automatic distillation and purification of environmental tritium analysis and can complete fully-automatic acquisition, preparation, distillation, purification, measurement and analysis of environmental tritium together with a tritium analysis meter, so that an environmental tritium analysis system is free of attendance in the entire process, and fully-automatic monitoring of regions with severe environmental tritium radiation is realized; and the automatic tritium extraction device greatly reduces manual intervention, so that monitoring results are more accurate, labor costs are saved, and the probability of physical harm to relevant service personnel is drastically lowered.
  • BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS
  • FIG. 1 is a flow structural diagram of the invention.
  • FIG. 2 is a collaboration diagram of a temperature control unit and a distillation chamber of the invention.
  • DETAILED DESCRIPTION OF THE INVENTION
  • To provide a better understanding of the technical solutions of the invention for those skilled in the art, the technical solutions of the embodiments of the invention will be clearly and completely described below in conjunction with the accompanying drawings of the embodiments. Obviously, the embodiments in the following description are merely illustrative ones, and are not all possible ones of the invention. All other embodiments obtained by those ordinarily skilled in the art without creative labor should also fall within the protection scope of the invention.
  • As shown in FIG. 1, 2, an automatic tritium extraction device for environmental monitoring comprises a distillation chamber 1, a temperature control unit 2, a condensation unit 4 and an auxiliary condensation unit 5, wherein a main part of the distillation chamber 1 is cylindrical, and the bottom of the distillation chamber 1 is conical; the temperature control unit 2 encircles one part of the outer wall of the main part of the distillation chamber 1 and is used to heat the distillation chamber 1; one end of the condensation unit 4 is connected to the top of the distillation chamber 1, and the other end of the condensation unit 4 is connected to a delivery pipe 3 at the top of the condensation unit 4; and the auxiliary condensation unit 5 is connected to the condensation unit 4 and is used to cyclically deliver a condensing agent into the condensation unit 4.
  • An upper part of the distillation chamber 1 is connected to multiple agent bottles through multiple pipes and a first pump 11, wherein cleaning agents or distilling agents are contained in the multiple bottles 15, and the first pump 11 may be a WK10 high-precision micro peristaltic pump capable of accurately regulating and controlling the delivery quantity. The upper part of the distillation chamber 1 is also connected to a sample tank 7 containing to-be-tested tritium-containing samples through a pipe and a second pump 12, wherein the second pump 12 is used to transport the tritium-containing samples into the distillation chamber 1. A sample outlet 14 is formed in the conical bottom of the distillation chamber 1 and is communicated with the outside through a third pump 13 to discharge the samples in the distillation chamber 1 to the outside.
  • As shown in FIG. 2, the temperature control unit 2 comprises heating elements 21 encircling the outer wall of the main part of the distillation chamber 1 and a temperature control switch 22 disposed between the heating elements 21 and the outer wall of the distillation chamber 1, wherein the heating elements 21 generate heat for distillation in the distillation chamber 1; and the temperature control switch 22 is used to sense the temperature of the outer wall surface of the distillation chamber 1 in real time, timely and automatically power on the heating elements 21 to heat the distillation chamber 1 when the temperature of the outer wall surface of the distillation chamber 1 is lower than a preset value 80-100° C., and timely and automatically power off the heating elements 21, when the temperature of the outer wall surface of the distillation chamber 1 is higher than the preset value 80-100° C., to maintain the temperature of the distillation chamber 1 at the preset value to ensure continuous and efficient distillation.
  • The condensation unit 4 comprises a hollow condensing agent circulation chamber 41 and a spiral heat-exchange tube 42 disposed in the condensing agent circulation chamber 41, wherein the spiral heat-exchange tube 42 allows tritium sample steam to circulate therein, the condensing agent circulation chamber 41 is filled with the condensing agent which may be deionized distilled water, the tritium sample steam in the spiral heat-exchange tube 42 is cooled and condensed into liquid by the condensing agent, an inlet 411 communicated with the delivery pipe 3 is formed in the top of the condensing agent circulation chamber 41, an outlet 412 communicated with an environmental tritium sample collection tank 6 may be formed in the bottom of the condensing agent circulation chamber 41, and an airtight container is formed by other parts of the condensing agent circulation chamber 41 to allow the condensing agent to circulate therein.
  • The auxiliary condensation unit 5 is used to control the condensing process of the condensation unit 4 and comprises a cavity 51 for storing the condensing agent, an upper tube 52 for communicating the cavity 51 with an upper part of the condensing agent circulation chamber 41, a lower tube 53 for communicating the cavity 51 with a lower part of the condensing agent circulation chamber 41, and a power device for driving the condensing agent to flow into the condensing agent circulation chamber 41 from the cavity 51 through the lower tube 53 or driving the condensing agent to flow into the cavity 51 from the condensing agent circulation chamber 41 through the upper tube 52, wherein the power device is a peristaltic pump or a diaphragm pump and is used to drive the condensing agent to cyclically flow between the condensing agent circulation chamber 41 and the cavity 51.
  • The delivery pipe 3 for guiding distillation gas generated in the distillation chamber 1 into the condensation unit 4 comprises a first vertical pipe 31 connected to the top of the distillation chamber 1, a second vertical pipe 32 connected to the top of the condensing agent circulation chamber 41, and an oblique pipe 33 obliquely connected between the first vertical pipe 31 and the second vertical pipe 32, wherein the top of the distillation chamber 1 is located on the same horizontal plane as the top of the condensing agent circulation chamber 41, and the oblique pipe 33 inclines upwards from the distillation chamber 1 to the condensation unit 4, that is, the second vertical pipe 32 is longer than the first vertical pipe 31.
  • A first spherical bulge 311 with a larger inner diameter is formed in the first vertical pipe 31, is close to the top of the distillation chamber 1 and is spaced from the top of the top of the distillation chamber 1 by a small distance, so that steam output from the top of the distillation chamber 1 passes through the first vertical pipe 31 with the inner diameter sharply decreased to form a micro positive pressure and then enters the first spherical bulge 311 with the larger inner diameter to form a micro negative pressure, in this way, sample drops carried by steam are prevented from entering the condensation unit 4 via the delivery pipe 3, and the monitoring accuracy of the environmental tritium samples is guaranteed.
  • A second spherical bulge 321 with a larger inner diameter is formed in the second vertical pipe 32, is close to the top of the condensing agent circulation chamber 41 and is spaced from the top of the condensing agent circulation chamber 41 by a small distance, so that steam entering the condensing agent circulation chamber 41 first passes through the second spherical bulge 321 with the inner diameter sharply increased to be pre-condensed and then enters the condensing agent circulation chamber 41 via the second vertical pipe 32 with a smaller inner diameter, thus improving the condensation efficiency.
  • After the automatic tritium extraction device is started, the distillation chamber 1 is automatically cleaned at first, then, the environmental tritium samples and the distilling agent enter the distillation chamber, the temperature control unit 2 is started to carry out controllable distillation, and steam enters the steam delivery pipe 3, wherein one part of the steam is condensed to flow back into the distillation chamber 1 to be re-distillated under the effect of the structure of the first spherical bulge 311 at a port of the first vertical pipe 31 and the oblique upward structure of the oblique pipe 33, and the other part of the steam enters the condensation unit 4 via the steam delivery pipe 3 and is mostly condensed in the spiral heat-exchange tube 42 in the condensing agent circulation chamber 41 under the effect of the structure and temperature to flow into the environmental tritium sample collection tank 6 under the effect of gravity; and the steam and the condensing agent exchange heat in the spiral heat-exchange tube 42, so that the temperature of the steam drops, the temperature of the condensing agent rises, the condensing agent with the temperature increased returns into the cavity 51 via the upper tube 52, and the low-temperature condensing agent in the cavity 51 enters the condensing agent circulation chamber 41 via the lower tube 53, and thus, the condensing capacity of the condensation unit 4 is guaranteed.
  • An automatic tritium extraction method for environmental monitoring comprises the following steps:
  • 1) Cleaning of a distillation chamber: a cleaning agent is used, a first pump is started to pump the cleaning agent into the distillation chamber, and the quantity of the cleaning agent pumped into the distillation chamber is accurately controlled; the temperature control unit is started to increase the temperature of the outer wall surface of the distillation chamber 1 to 80-100° C.; a third pump is started to deliver outside air into the distillation chamber 1 to agitate the cleaning agent to clean the distillation chamber 1, and at this moment, a second pump and a condensation unit are stopped; and when agitation cleaning of the distillation chamber is completed a period of time later, the third pump is started again to discharge mixed liquor in the distillation chamber 1 out of the distillation chamber 1 via a sample outlet 14;
  • 2) Distillation rinsing: the cleaning agent is replaced with a distilling agent, the second pump is started to pump a specified quantity of samples, namely one third of samples in a sample tank 7, into the distillation chamber 1; then, the first pump is started to pump a specified quantity of the distilling agent, in proportion with the one third of the samples, into the distillation chamber 1 from different bottles; the samples and the distilling agent are mixed; and the temperature control unit is kept in the on-state to maintain the temperature of the outer wall surface of the distillation chamber 1 at 80-100° C.;
  • 3) Distillation: a collection tank containing environmental tritium finished products in step 2) is replaced with an empty collection tank, and the second pump further pumps one third of samples into the distillation chamber 1 from the sample tank 7; the first pump is started to pump a specified quantity of the distilling agent, in proportion with the one third of samples, into the distillation chamber 1 from different bottles; and temperature control unit is kept in the on-state to maintain the temperature of the outer wall surface of the distillation chamber 1 at 80-100° C. and is stopped when the distillation amount reaches a preset value 500-700 mL;
  • 4) Carrying out condensation when Step 2) and Step 3) are performed: an auxiliary condensation unit is started, a power device delivers a condensing agent into a condensing agent circulation chamber 41 from a cavity via a lower tube 53 and recovers the condensing agent subjected to heat exchange in the condensing agent circulation chamber 41 back into the cavity 51 via an upper tube in the direction of arrow;
  • 5) Discharging samples out of the distillation chamber: the second pump further pumps the last one third of samples into the distillation chamber 1 from the sample tank 7; and the first pump is stopped, and the third pump is started to discharge all the samples 1 in the distillation chamber 1 out of the distillation chamber 1 via the sample outlet 14; and
  • 6) Monitoring: liquid environmental tritium finished products in the collection tank 6 are measured and analyzed by a tritium analysis meter.
  • The above specific embodiments are merely used to explain the invention, and are not intended to limit the invention. Any modifications or transformations of the invention made on the basis of the spirit of the invention and within the protection scope of the claims should also fall within the protection scope of the invention.

Claims (2)

What is claimed is:
1. An automatic tritium extraction method for environmental monitoring, comprising the following steps:
1) cleaning of a distillation chamber: a cleaning fluid is used, a first pump is started to pump a specified quantity of the cleaning fluid into the distillation chamber, a temperature control unit is started to heat the distillation chamber to a preset temperature, then a third pump is started to deliver outside air into the distillation chamber, and when agitation cleaning of the distillation chamber is completed, mixed liquor in the distillation chamber is discharged by the third pump;
2) distillation rinsing: a distilling fluid is used, a second pump is started to pump a specified quantity of samples into the distillation chamber, then, the first pump is started to pump a specified quantity of the distilling fluid into the distillation chamber, and the temperature control unit is started to maintain the temperature of an outer wall of the distillation chamber at the preset temperature, and a collection tank containing finished products is replaced with an empty collection tank;
3) distillation: the distilling fluid is used, the second pump further pumps a specified quantity of samples into the distillation chamber, the first pump is started to pump a specified quantity of the distilling fluid into the distillation chamber, and the temperature control unit is started to maintain the distillation chamber at a preset temperature and is stopped when the distillation amount reaches a preset value;
4) carrying out condensation when Step 2) and Step 3) are performed: an auxiliary condensation unit is started, and a condensing agent is delivered into a condensing agent circulation chamber via a lower tube and flows back into a cavity via an upper tube after being subjected to heat exchange in the condensing agent circulation chamber;
5) discharging samples out of the distillation chamber: the second pump further pumps the rest of samples in a sample tank into the distillation chamber, and the third pump is started to discharge all the samples out of the distillation chamber.
2. The automatic tritium extraction method for environmental monitoring according to claim 1, wherein the preset temperature in Step 1) and Step 2) is 80-100° C., and the preset value in Step 3) is 500-700 mL.
US17/523,486 2019-06-10 2021-11-10 Automatic tritium extraction method for environmental monitoring Abandoned US20220111304A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US17/523,486 US20220111304A1 (en) 2019-06-10 2021-11-10 Automatic tritium extraction method for environmental monitoring

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
CN201910496784.4 2019-06-10
CN201910496784.4A CN110180199B (en) 2019-06-10 Tritium automatic extraction device and method for environmental monitoring
US16/896,689 US11202972B2 (en) 2019-06-10 2020-06-09 Automatic tritium extraction device and method for environmental monitoring
US17/523,486 US20220111304A1 (en) 2019-06-10 2021-11-10 Automatic tritium extraction method for environmental monitoring

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
US16/896,689 Division US11202972B2 (en) 2019-06-10 2020-06-09 Automatic tritium extraction device and method for environmental monitoring

Publications (1)

Publication Number Publication Date
US20220111304A1 true US20220111304A1 (en) 2022-04-14

Family

ID=67721029

Family Applications (2)

Application Number Title Priority Date Filing Date
US16/896,689 Active US11202972B2 (en) 2019-06-10 2020-06-09 Automatic tritium extraction device and method for environmental monitoring
US17/523,486 Abandoned US20220111304A1 (en) 2019-06-10 2021-11-10 Automatic tritium extraction method for environmental monitoring

Family Applications Before (1)

Application Number Title Priority Date Filing Date
US16/896,689 Active US11202972B2 (en) 2019-06-10 2020-06-09 Automatic tritium extraction device and method for environmental monitoring

Country Status (1)

Country Link
US (2) US11202972B2 (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4119560A (en) * 1977-03-28 1978-10-10 United Technologies Corporation Method of treating radioactive waste
US4246233A (en) * 1978-08-23 1981-01-20 United Technologies Corporation Inert carrier drying and coating apparatus
US4314877A (en) * 1979-11-02 1982-02-09 Kraftwerk Union Aktiengesellschaft Method and apparatus for drying radioactive waste water concentrates from evaporators
US4892684A (en) * 1986-11-12 1990-01-09 Harp Richard J Method and apparatus for separating radionuclides from non-radionuclides
US4902446A (en) * 1984-08-31 1990-02-20 Siemens Aktiengesellschaft Method for reducing the volume of radioactively loaded liquids, and finned body for use in the process
WO2008081468A1 (en) * 2007-01-03 2008-07-10 Council Of Scientific & Industrial Research Tritium injection technique for the estimation of natural groundwater recharge
US20140151215A1 (en) * 2012-11-30 2014-06-05 Korea Atomic Energy Research Institute Separation and Recovery Device for Liquid Waste Including Radionuclide, and Separation and Recovery Method Using the Same

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1725528A (en) * 1927-04-15 1929-08-20 Konter Michael Distillation apparatus
US3864214A (en) * 1972-11-07 1975-02-04 Evald Ohakas Apparatus for the Plural Stage Distillation of Drinking Alcohol
DE102011121650A1 (en) * 2011-12-19 2013-06-20 Hans Heidolph Gmbh & Co. Kg distillation apparatus

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4119560A (en) * 1977-03-28 1978-10-10 United Technologies Corporation Method of treating radioactive waste
US4246233A (en) * 1978-08-23 1981-01-20 United Technologies Corporation Inert carrier drying and coating apparatus
US4314877A (en) * 1979-11-02 1982-02-09 Kraftwerk Union Aktiengesellschaft Method and apparatus for drying radioactive waste water concentrates from evaporators
US4902446A (en) * 1984-08-31 1990-02-20 Siemens Aktiengesellschaft Method for reducing the volume of radioactively loaded liquids, and finned body for use in the process
US4892684A (en) * 1986-11-12 1990-01-09 Harp Richard J Method and apparatus for separating radionuclides from non-radionuclides
WO2008081468A1 (en) * 2007-01-03 2008-07-10 Council Of Scientific & Industrial Research Tritium injection technique for the estimation of natural groundwater recharge
US20140151215A1 (en) * 2012-11-30 2014-06-05 Korea Atomic Energy Research Institute Separation and Recovery Device for Liquid Waste Including Radionuclide, and Separation and Recovery Method Using the Same
US9604154B2 (en) * 2012-11-30 2017-03-28 Korea Atomic Energy Research Institute Separation and recovery device for liquid waste including radionuclide, and separation and recovery method using the same

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
N.P Kherani, "An alternative approach to tritium-in-water monitoring", Nuclear Instruments and Methods in Physics Research Section A: Accelerators, Spectrometers, Detectors and Associated Equipment, 2002, Pages 650-659, ISSN 0168-9002, https://doi.org/10.1016/S0168-9002(01)02008-3. *

Also Published As

Publication number Publication date
US20200384382A1 (en) 2020-12-10
US11202972B2 (en) 2021-12-21
CN110180199A (en) 2019-08-30

Similar Documents

Publication Publication Date Title
CN111721956A (en) Liquid path system of full-automatic biochemical analyzer
CN219608910U (en) Water quality monitoring device based on quantitative concentration
CN112462082A (en) Automatic sample adding system and automatic sample adding method
US11202972B2 (en) Automatic tritium extraction device and method for environmental monitoring
CN205413827U (en) Biochemical analyzer liquid way system
CN201083641Y (en) Liquid analytical equipment
CN110180199B (en) Tritium automatic extraction device and method for environmental monitoring
CN102778383B (en) Automatic solution diluting equipment
CN208902751U (en) Quantitative sample injection and cleaning system
CN210448127U (en) Automatic tritium extraction device for environmental monitoring
CN209946178U (en) Liquid path system of full-automatic biochemical analyzer
CN213986175U (en) Novel full-automatic salt and iodine analyzer
CN211885434U (en) Novel double water distiller
CN104280513B (en) A kind of water sample detection reaction tank
CN220982836U (en) Cyanide detects appearance preprocessing device
CN102175507B (en) On-line concentration system suitable for large-flow enriching instrument
CN109270284A (en) Quantitative sample injection and cleaning system
CN110220767B (en) Automatic concentration device for water radionuclide
CN218610858U (en) Traditional chinese medicine draws equipment CIP cleaning system
CN111849749B (en) High-efficient piece-rate system of adult toy cardiac muscle cell
CN204188587U (en) A kind of water sample detection reaction tank
CN214346434U (en) Device for quickly adjusting pH value of in-vitro diagnostic reagent
CN219266268U (en) Low turbidity sensor calibration device in batches
CN221713596U (en) Full-automatic distillation equipment
CN114113571B (en) Immunoassay analyzer, liquid path system thereof and cleaning method of liquid path system

Legal Events

Date Code Title Description
STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: FINAL REJECTION MAILED

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION