CN106967882A - A kind of method that use polyamide extracts technetium from molybdenum solution - Google Patents
A kind of method that use polyamide extracts technetium from molybdenum solution Download PDFInfo
- Publication number
- CN106967882A CN106967882A CN201710027854.2A CN201710027854A CN106967882A CN 106967882 A CN106967882 A CN 106967882A CN 201710027854 A CN201710027854 A CN 201710027854A CN 106967882 A CN106967882 A CN 106967882A
- Authority
- CN
- China
- Prior art keywords
- technetium
- polyamide
- molybdenum
- solution
- extracts
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/22—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
- C22B3/24—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition by adsorption on solid substances, e.g. by extraction with solid resins
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B61/00—Obtaining metals not elsewhere provided for in this subclass
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The invention belongs to radionuclide separation field, and in particular to a kind of method that use polyamide extracts technetium from molybdenum solution.Methods described comprises the following steps:(1) prepare hydroxide ion concentration and be more than or equal to 1mol/L molybdenum and the mixed solution of technetium;(2) using the technetium in the molybdenum technetium mixed solution obtained by polyamide adsorption step (1);(3) molybdenum of a small amount of adhesive tape in polyamide surface is washed using cleaning solution;(4) leacheate for being less than 1mol/L using hydroxide ion concentration desorbs the technetium of polyamide adsorption.Methods described has solid phase separation material radiation resistance good, and adsorption separation performance is stable, and solid phase separation material is cheap the characteristics of be easy to get.
Description
Technical field
The invention belongs to radionuclide separation field, and in particular to one kind is extracted using polyamide from molybdenum solution
The method of technetium.
Background technology
99mTc is because the advantages of its purer low-energyγ-ray (141keV), shorter half-life period (6.03h) and as mesh
One of the most frequently used radionuclide in preceding nuclear medicine.At present,99mTc mainly passes through99Mo/99mTc chromatographs generator is obtained.In hair
In raw device, parent nuclide99Mo decays are obtained99mTc efficiency is 88.6%, and remaining 11.4% directly decay to99Tc.It is this99Mo/99mTc generators, can be by daughter nuclide99mTc(T1/2=6h) from parent nuclide99Mo(T1/2=66.7h) in extract
Come.In this manner it is possible to which by long-distance transport, Short-lived radionuclide is provided for the area away from nuclear facilities99mTc, and
Daily elution can be accomplished99mTc, as milk cow milking.Therefore,99Mo/99mTc generators are also known as " molybdenum technetium cow ".
The presently commercially available clinical application that is used for99Mo/99mTc generators are used99Mo is substantially all using fission99Mo,
Its manufacture method is that neutron bombardment uranium -235 are used in reactor, and high specific activity is manufactured by the fission of uranium -23599Mo.These
Fission99Mo is main by a few government in the world is all or supports research reactor (NRU, Canada;HFR, Holland;BR2, than
When sharp;Osiris, France;Safari, South Africa etc.) provided.
Fissioned at present99In Mo supply process, the reactor existed in a series of problems, including above-mentioned supply chain needs
Slightly enriched uranium target is transformed into from high-enriched uranium target, this transfer process can cause supply unstable or reduce supply;Fission99Mo life
Production mode can produce substantial amounts of Long-lived Radionuclides, and Environmental costs are too high;Under the theory effect of " full payment recovery ",99Mo price can continuous rise;The customary or unexpected shutdown of reactor in above-mentioned supply chain causes99Mo is in short supply.Cause
This, starts actively to find newly in industry99Mo and99mTc acquisition modes.
Other can be prepared99Mo method has been widely studied, including based on thermal capture99Mo manufacturing technologies;Base
In100Mo (γ, n)99Mo reactions99Mo manufacturing technologies;It is based on100Mo (p, pn)99Mo reactions99Mo manufacturing technologies;It is based on100Mo
(n, nn)99Mo reactions99Mo manufacturing technologies;Also passing through based on accelerator100Mo is directly produced99mTc technology.Fission99It is a kind of DNAcarrier free that the characteristics of Mo, which is mainly him,99Mo, that is to say, that fission99Other Mo same position is practically free of in Mo
Element.Other can be prepared99The characteristics of Mo method has individual common, is obtained99Mo is containing carrier99Mo, i.e.,99Contain in Mo
Other Mo isotope.This also causes what is obtained99Mo specific activity is very low, it is impossible to by from fission99Separation and Extraction in Mo99mTc method is obtained99mTc.Therefore, how from low specific activity99Separation and Extraction in Mo99mTc turns into key.
In order to from low specific activity99Extracted in Mo and meet clinical requirement99mTc, has carried out substantial amounts of research.Low ratio is lived
Degree99mTc extractive technique can be divided into for four generations:Solvent extraction, sublimed method, electrochemical process, and Column chromatography.Column chromatography
Be critical that with a kind of solid phase material from containing99Mo and99mAdsorbed in Tc solution99mTc, without adsorbing or seldom inhaling
It is attached99Mo, so as to realize the separation of molybdenum and technetium.This method, which has, easily realizes automation, the characteristics of reliable and stable, therefore turns into
The focus of research.
There is the method for using ABEC-2000 as solid phase separation material in the prior art, also have using the He of Dowex-1 × 8
ABEC-2000 as solid absorbent materials Separation of Molybdenum and technetium research.Wherein, made using the anion exchange resin of Dowex-1 × 8
Organic solvent or perchloric acid is needed to use to be eluted for the solid phase material of Separation of Molybdenum and technetium, could be by technetium from solid phase material
Desorption is got off, and this has risk for Clinical practice.ABEC-2000 also has some shortcomings, such as its radiation-resistant property is poor, material
Material is complicated, and the chromatograph post uniformity manufactured with it is poor.
The content of the invention
The problem of in background technology, technetium is extracted from molybdenum solution the invention provides a kind of use polyamide
Method.The present invention uses polyamide as the solid phase separation material of molybdenum and technetium, and optimizes the process and ginseng of separating technology
Number, can adsorb technetium from the mixed solution containing molybdenum and technetium, without adsorbing or seldom adsorbing molybdenum, and can be desorbed using rinsing liquid
Technetium, so as to realize the separation of molybdenum and technetium.Methods described has that solid phase separation material radiation resistance is good, and adsorption separation performance is steady
Fixed, solid phase separation material is cheap the characteristics of be easy to get.
To achieve the above object, the present invention proposes following technical scheme:
A kind of method that use polyamide extracts technetium from molybdenum solution, methods described comprises the following steps:
(1) prepare hydroxide ion concentration and be more than or equal to 1mol/L molybdenum and the mixed solution of technetium;
(2) using the technetium in the molybdenum technetium mixed solution obtained by polyamide adsorption step (1);
(3) molybdenum of a small amount of adhesive tape in polyamide surface is washed using cleaning solution;
(4) leacheate for being less than 1mol/L using hydroxide ion concentration desorbs the technetium of polyamide adsorption.
Further, in the step (1), the hydroxide ion concentration of the mixed solution of the molybdenum and technetium, preferably 3-
6mol/L。
Further, the polyamide is polyamide -6 (PA6), polyamide -66 (PA66), polyamide-11
(PAll), polyamide -12 (PAl2), polyamide -46 (PA46), polyamide -610 (PA610), polyamide -612 (PA612) and
One or more in polyamide -1010 (PA1010).
Further, the granularity of the polyamide, preferably 50-1000 mesh.
Further, the granularity of the polyamide, preferably 100-500 mesh.
Further, the cleaning solution is arbitrarily matched containing carbanion, bicarbonate ion, hydroxide ion
Solution.
Further, the cleaning solution is preferably 3-6mol/L NaOH solution.
Further, the preferred sterilized water for injection of the rinsing liquid.
The beneficial effects of the present invention are:
The invention provides a kind of method that use polyamide extracts technetium from molybdenum solution.The present invention looks for another way,
It is preferred that solid phase separation material of the polyamide as molybdenum and technetium, and optimize the process and parameter of separating technology, Neng Goucong
Hydroxide ion concentration, which is more than or equal to, adsorbs technetium containing in molybdenum solution for 1mol/L, without adsorbing or seldom adsorbing molybdenum.And use hydrogen
The aqueous solution that oxygen ion concentration is less than 1mol/L can desorb technetium.So as to realize the separation of molybdenum and technetium.And this method has admittedly
Phase separation material radiation resistance is good, and adsorption separation performance is stable, and solid phase separation material is cheap the characteristics of be easy to get.
The polyamide used in the present invention includes polyamide -6 (PA6), polyamide -66 (PA66), polyamide-11
(PAll), polyamide -12 (PAl2), polyamide -46 (PA46), polyamide -610 (PA610), polyamide -612 (PA612) and
Polyamide -1010 (PA1010) etc..This resin contains abundant amide groups, can with water or other can form the thing of hydrogen bond
Hydrogen bond action occurs for matter, and it shows hydrophily in water.In this application, it exactly make use of this property and realize the de- of technetium
It is attached.
Embodiment
The present invention provides a kind of method that use polyamide extracts technetium from molybdenum solution, and methods described includes following step
Suddenly:
(1) prepare hydroxide ion concentration and be more than or equal to 1mol/L molybdenum and the mixed solution of technetium;
It is different according to the source of molybdenum, prepare the mixed solution of molybdenum of the hydroxide ion concentration more than or equal to 1mol/L and technetium
Method is also different.For example there is carrier for what is prepared using thermal neutron activated method99Mo, its target material is molybdenum oxide, can be with
Use the sodium hydroxide of high concentration or other highly basic dissolving oxidation molybdenum target so that the hydroxide ion concentration in the solution of acquisition is big
In equal to 1mol/L.For low specific activity99When Mo preparation uses metal molybdenum target, the hydrogen-oxygen of high concentration can also be used
Change sodium or the dissolving of other highly basic adds appropriate hydrogen peroxide dissolving molybdenum target so that the hydroxide ion concentration in the solution of acquisition is more than
Equal to 1mol/L.
The molybdenum target both can be natural molybdenum or its oxide or enrichment molybdenum or its oxide.
The hydroxide ion concentration requirement is more than or equal to 1mol/L, preferably 3-6mol/L.
Ensure that the purpose that hydroxide ion concentration is more than or equal to 1mol/L there are two, one is as hydroxide ion is more than 1
Afterwards, concentration is bigger, and polyamide is bigger to the adsorption capacity of technetium, and two be polyamide after pH value of solution is more than 13
Hardly adsorb or seldom adsorb molybdenum.
(2) technetium in molybdenum technetium mixed solution is adsorbed using polyamide;
The step can use dynamic method Separation of Molybdenum technetium mixed solution.Quality is prepared using the polyamide of certain mass
Layer post carries out Dynamic adsorption molybdenum technetium.For example it is with certain flow rate that molybdenum technetium mixed solution pump is excessively poly- using peristaltic pump or syringe pump
Acid amides chromatograph post so that the technetium in molybdenum technetium mixed solution is attracted on polyamide chromatograph post, and molybdenum is not adsorbed or few
It is attracted on chromatograph post.Largely99Mo flows out after chromatograph post, treats99Mo decay daughter99mThe step is repeated after Tc generations
Suddenly, it is possible to which Separation of Molybdenum technetium is obtained again99mTc。
The step can also use static method Separation of Molybdenum and technetium from molybdenum technetium mixed solution.For example can be by polyamide
Put into molybdenum technetium mixed solution, after balance to be adsorbed, separation of solid and liquid, so as to realize that molybdenum technetium is separated.
The polyamide is the family macromolecule compound being polymerized by amide groups, and what is used in the present invention is poly-
Amide resin is polyamide -6 (PA6), polyamide -66 (PA66), polyamide-11 (PAll), polyamide -12 (PAl2), polyamides
One in amine -46 (PA46), polyamide -610 (PA610), polyamide -612 (PA612) and polyamide -1010 (PA1010) etc.
Plant or a variety of mixtures.That is, the polyamide used in the present invention can be a kind of single polyamide, also may be used
To be the mixture of a variety of polyamide composition.This resin contains abundant amide groups, can with water or other can form hydrogen
Hydrogen bond action occurs for the material of key, and it shows hydrophily in water.In this application, it exactly make use of this property and realize
The desorption of technetium.
The particle size range of the polyamide is the mesh of 50 mesh -1000, preferably the mesh of 100 mesh -500.
The quality of the polyamide depends primarily on the volume for the molybdenum technetium mixed solution for needing adsorbing separation.For this
For the application in field, quality is usually 0.1g-20g.
(3) molybdenum of a small amount of adhesive tape in polyamide surface is washed using cleaning solution;
Adsorbed technetium polyamide surface can adhesive tape some molybdenums, a kind of cleaning solution can be used to remove these molybdenums, together
When ensure absorption technetium be not desorbed.Polyamide for adsorbing technetium using dynamic adsorption method, can be excessively certain with pump
The cleaning solution of volume, the polyamide for being adsorbed technetium using static adsorptive method can be washed polyamide input
Liquid is washed, rinsing is multiple.
The cleaning solution includes containing any of carbanion, bicarbonate ion, hydroxide ion or appointed many
Plant the solution of ion.Preferably concentration is 3-6mol/L sodium hydrate aqueous solution.
The factors such as the consumption of the wash solution and the consumption of polyamide are relevant, while molybdenum is washed away as far as possible,
It should be guaranteed that and wash technetium off less as far as possible.
(4) leacheate for being less than 1mol/L using hydroxide ion concentration desorbs the technetium of polyamide adsorption;
Polyamide for adsorbing technetium using dynamic adsorption method, can cross the leacheate of certain volume with pump.It is right
In the polyamide that technetium is adsorbed using static adsorptive method, polyamide can be put into leacheate, rinsing is multiple.
Hydroxide ion concentration in the leacheate is less than 1mol/L, preferably sterilized water for injection.
The volume and rinsing times for the leacheate that the pump is crossed, it shall be guaranteed that the technetium adsorbed on post is eluted completely as far as possible.
For the ease of being further appreciated that to the present invention, examples provided below has done more detailed description to it.This
A little embodiments are not used for limiting the scope of the present invention or implementation principle only for narration, and protection scope of the present invention is still with right
It is required that be defined, including made on this basis obvious changes or variations etc..
Embodiment 1:
It is slowly added in Native Oxide molybdenum powders of 6mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 4.6mol/L in the solution obtained.Chromatograph post is made using the mesh PA6 of 3g 200, with 10mL/min flow velocity
Mixed solution pump containing molybdenum technetium is crossed into chromatograph post, efflux containing molybdenum is reclaimed.Now, technetium is attracted on chromatograph post.Use
5mol/L NaOH solution, the chromatograph post is crossed with 10mL/min flow pump, washs the molybdenum of a small amount of adhesive tape thereon.Finally, with
10mL/min flow velocity, the technetium that pump is crossed on 10mL sterilizeds water for injection elution post.The eluent of acquisition is the solution containing technetium,
Complete the separation of molybdenum and technetium.
Embodiment 2:
It is slowly added in Native Oxide molybdenum powders of 6mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 4.6mol/L in the solution obtained.Chromatograph post is made using the mesh PA66 of 3g 200, with 10mL/min stream
Mixed solution pump containing molybdenum technetium is crossed chromatograph post by speed, reclaims efflux containing molybdenum.Now, technetium is attracted on chromatograph post.Use
20mL5mol/L NaOH solution, the chromatograph post is crossed with 10mL/min flow pump, washs the molybdenum of a small amount of adhesive tape thereon.Finally,
With 10mL/min flow velocity, the technetium that pump is crossed on 10mL sterilizeds water for injection elution post.The eluent of acquisition is to contain the molten of technetium
Liquid, completes the separation of molybdenum and technetium.
Embodiment 3:
It is slowly added in Native Oxide molybdenum powders of 4mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 2.6mol/L in the solution obtained.Using 1g 200 mesh PA46 and 2g 200 mesh PA66 mixing, color is made
Layer post, chromatograph post is crossed with 10mL/min flow velocity by the mixed solution pump containing molybdenum technetium, reclaims efflux containing molybdenum.Now, technetium quilt
Absorption is on chromatograph post.Using 20mL 5mol/L NaOH solution, the chromatograph post is crossed with 10mL/min flow pump, it is washed
The molybdenum of upper a small amount of adhesive tape.Finally, with 10mL/min flow velocity, the technetium that pump is crossed on 10mL sterilizeds water for injection elution post.Obtain
Eluent is the solution containing technetium, completes the separation of molybdenum and technetium.
Embodiment 4:
It is slowly added in Native Oxide molybdenum powders of 6mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 4.6mol/L in the solution obtained.Chromatograph post is made using the mesh PA66 of 1g 200, with 10mL/min stream
Mixed solution pump containing molybdenum technetium is crossed chromatograph post by speed, reclaims efflux containing molybdenum.Now, technetium is attracted on chromatograph post.Use
20mL 5mol/L NaOH solution, the chromatograph post is crossed with 10mL/min flow pump, washs the molybdenum of a small amount of adhesive tape thereon.Finally,
With 10mL/min flow velocity, the technetium that pump is crossed on 10mL sterilizeds water for injection elution post.The eluent of acquisition is to contain the molten of technetium
Liquid, completes the separation of molybdenum and technetium.
Embodiment 5:
It is slowly added in Native Oxide molybdenum powders of 6mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 4.6mol/L in the solution obtained.Chromatograph post is made using 3g800 mesh PA66, with 2mL/min flow velocity
Mixed solution pump containing molybdenum technetium is crossed into chromatograph post, efflux containing molybdenum is reclaimed.Now, technetium is attracted on chromatograph post.Use
20mL5mol/L NaOH solution, the chromatograph post is crossed with 2mL/min flow pump, washs the molybdenum of a small amount of adhesive tape thereon.Finally, with
2mL/min flow velocity, the technetium that pump is crossed on 10mL sterilizeds water for injection elution post.The eluent of acquisition is the solution containing technetium,
Complete the separation of molybdenum and technetium.
Embodiment 6:
It is slowly added in Native Oxide molybdenum powders of 6mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 4.6mol/L in the solution obtained.Chromatograph post is made using the mesh PA66 of 3g 200, with 10mL/min stream
Mixed solution pump containing molybdenum technetium is crossed chromatograph post by speed, reclaims efflux containing molybdenum.Now, technetium is attracted on chromatograph post.Use
20mL1mol/L sodium carbonate liquor, the chromatograph post is crossed with 10mL/min flow pump, washs the molybdenum of a small amount of adhesive tape thereon.Most
Afterwards, with 10mL/min flow velocity, the technetium that pump is crossed on 10mL sterilizeds water for injection elution post.The eluent of acquisition is to contain technetium
Solution, completes the separation of molybdenum and technetium.
Embodiment 7:
It is slowly added in Native Oxide molybdenum powders of 6mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 4.6mol/L in the solution obtained.Chromatograph post is made using the mesh PA66 of 3g 200, with 10mL/min stream
Mixed solution pump containing molybdenum technetium is crossed chromatograph post by speed, reclaims efflux containing molybdenum.Now, technetium is attracted on chromatograph post.Use
20mL3mol/L NaOH solution, the chromatograph post is crossed with 10mL/min flow pump, washs the molybdenum of a small amount of adhesive tape thereon.Finally,
With 10mL/min flow velocity, the technetium that pump is crossed on 10mL sterilizeds water for injection elution post.The eluent of acquisition is to contain the molten of technetium
Liquid, completes the separation of molybdenum and technetium.
Embodiment 8:
It is slowly added in Native Oxide molybdenum powders of 6mol/L NaOH aqueous solution 50mL to the 5g after thermal neutron activated,
Molybdenum oxide powder is made fully to dissolve, it is therein99Mo is decayed into99mTc and99Tc, obtains the mixed solution containing molybdenum and technetium.Obtained
Hydroxide ion concentration is 4.6mol/L in the solution obtained.Chromatograph post is made using the mesh PA66 of 3g 200, with 10mL/min stream
Mixed solution pump containing molybdenum technetium is crossed chromatograph post by speed, reclaims efflux containing molybdenum.Now, technetium is attracted on chromatograph post.Use
20mL5mol/L NaOH solution, the chromatograph post is crossed with 10mL/min flow pump, washs the molybdenum of a small amount of adhesive tape thereon.Finally,
With 10mL/min flow velocity, the technetium that pump is crossed on the sodium hydroxide solution elution post that 10mLpH values are 12.The eluent of acquisition is
Solution containing technetium, completes the separation of molybdenum and technetium.
The influence of table 1, different separating technology to the yield of technetium and the residual quantity of molybdenum
Claims (8)
1. a kind of method that use polyamide extracts technetium from molybdenum solution, it is characterised in that:Methods described includes following step
Suddenly:
(1) prepare hydroxide ion concentration and be more than or equal to 1mol/L molybdenum and the mixed solution of technetium;
(2) using the technetium in the molybdenum technetium mixed solution obtained by polyamide adsorption step (1);
(3) molybdenum of a small amount of adhesive tape in polyamide surface is washed using cleaning solution;
(4) leacheate for being less than 1mol/L using hydroxide ion concentration desorbs the technetium of polyamide adsorption.
2. the method that a kind of use polyamide according to claim 1 extracts technetium from molybdenum solution, it is characterised in that:
In the step (1), the hydroxide ion concentration of the mixed solution of the molybdenum and technetium, preferably 3-6mol/L.
3. the method that a kind of use polyamide according to claim 1 extracts technetium from molybdenum solution, it is characterised in that:
The polyamide is polyamide -66 (PA66), polyamide-11 (PAll), polyamide -12 (PAl2), polyamide -46
(PA46), polyamide -6 (PA6), polyamide -610 (PA610), polyamide -612 (PA612) and polyamide -1010 (PA1010)
In one or more.
4. the method that a kind of use polyamide according to claim 3 extracts technetium from molybdenum solution, it is characterised in that:
The granularity of the polyamide, preferably 50-1000 mesh.
5. the method that a kind of use polyamide according to claim 4 extracts technetium from molybdenum solution, it is characterised in that:
The granularity of the polyamide, preferably 100-500 mesh.
6. the method that a kind of use polyamide according to claim 1 extracts technetium from molybdenum solution, it is characterised in that:
The cleaning solution is the solution arbitrarily matched containing carbanion, bicarbonate ion, hydroxide ion.
7. the method that a kind of use polyamide according to claim 6 extracts technetium from molybdenum solution, it is characterised in that:
The cleaning solution is preferably 3-6mol/L NaOH solution.
8. the method that a kind of use polyamide according to claim 1 extracts technetium from molybdenum solution, it is characterised in that:
The preferred sterilized water for injection of rinsing liquid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710027854.2A CN106967882B (en) | 2017-01-16 | 2017-01-16 | A method of technetium being extracted from molybdenum solution using polyamide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710027854.2A CN106967882B (en) | 2017-01-16 | 2017-01-16 | A method of technetium being extracted from molybdenum solution using polyamide |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106967882A true CN106967882A (en) | 2017-07-21 |
CN106967882B CN106967882B (en) | 2018-10-12 |
Family
ID=59334754
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710027854.2A Active CN106967882B (en) | 2017-01-16 | 2017-01-16 | A method of technetium being extracted from molybdenum solution using polyamide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106967882B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110923480A (en) * | 2019-12-20 | 2020-03-27 | 华中科技大学 | Application of aminoimidazole type ionic liquid loaded resin in adsorption separation of rhenium or technetium |
CN111485123A (en) * | 2020-04-13 | 2020-08-04 | 中国科学院近代物理研究所 | Separation from large-amount and low-specific-activity Mo solution99mTc device and method |
CN111500861A (en) * | 2020-04-01 | 2020-08-07 | 原子高科股份有限公司 | Method for extracting technetium from neutral molybdenum solution by using activated carbon fiber |
CN113509750A (en) * | 2020-04-10 | 2021-10-19 | 成都中核高通同位素股份有限公司 | Molybdenum-technetium separation column and molybdenum-technetium separation method |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090155167A1 (en) * | 2005-10-10 | 2009-06-18 | Ge Healthcare Limited | Automated method |
CN103650061A (en) * | 2011-07-13 | 2014-03-19 | 马林克罗特有限公司 | Process for producing Tc-99m |
-
2017
- 2017-01-16 CN CN201710027854.2A patent/CN106967882B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090155167A1 (en) * | 2005-10-10 | 2009-06-18 | Ge Healthcare Limited | Automated method |
CN103650061A (en) * | 2011-07-13 | 2014-03-19 | 马林克罗特有限公司 | Process for producing Tc-99m |
Non-Patent Citations (3)
Title |
---|
孙素元主编: "《放射性同位素发生器 译文集》", 31 December 1981, 原子能出版社 * |
王文渊等主编: "《分析化学 新版》", 31 July 2016, 华中科技大学出版社 * |
范我等主编: "《核药学教程》", 31 July 2005, 哈尔滨工程大学出版社 * |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110923480A (en) * | 2019-12-20 | 2020-03-27 | 华中科技大学 | Application of aminoimidazole type ionic liquid loaded resin in adsorption separation of rhenium or technetium |
CN111500861A (en) * | 2020-04-01 | 2020-08-07 | 原子高科股份有限公司 | Method for extracting technetium from neutral molybdenum solution by using activated carbon fiber |
CN111500861B (en) * | 2020-04-01 | 2021-11-05 | 原子高科股份有限公司 | Method for extracting technetium from neutral molybdenum solution by using activated carbon fiber |
CN113509750A (en) * | 2020-04-10 | 2021-10-19 | 成都中核高通同位素股份有限公司 | Molybdenum-technetium separation column and molybdenum-technetium separation method |
CN111485123A (en) * | 2020-04-13 | 2020-08-04 | 中国科学院近代物理研究所 | Separation from large-amount and low-specific-activity Mo solution99mTc device and method |
CN111485123B (en) * | 2020-04-13 | 2022-04-19 | 中国科学院近代物理研究所 | Separation from large-amount and low-specific-activity Mo solution99mTc device and method |
Also Published As
Publication number | Publication date |
---|---|
CN106967882B (en) | 2018-10-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106967882B (en) | A method of technetium being extracted from molybdenum solution using polyamide | |
CN106995882A (en) | A kind of method that use absorbent charcoal material extracts technetium from molybdenum solution | |
US7138643B2 (en) | Method and apparatus for separating ions of metallic elements in aqueous solution | |
CN111485123B (en) | Separation from large-amount and low-specific-activity Mo solution99mTc device and method | |
Chakravarty et al. | Nanomaterial-based adsorbents: the prospect of developing new generation radionuclide generators to meet future research and clinical demands | |
CN106198165B (en) | A kind of fast separation device and method of activation products americium uranium gallium | |
Zhang et al. | SPEC: A new process for strontium and cesium partitioning utilizing two macroporous silica-based supramolecular recognition agents impregnated polymeric composites | |
US8781055B2 (en) | Method and system for radioisotope generation | |
CN103263849A (en) | Rapid separation method of activated product gallium in fission product | |
TW201201844A (en) | Gallium-68 radioisotope generator and generating method thereof | |
Momoshima et al. | Analytical procedure for technetium-99 in seawater by ICP-MS | |
CN106048219B (en) | A kind of fast separation device and method of activation products uranium and gallium | |
Ramanujam et al. | Separation of carrier-free 90 Y from high level waste by supported liquid membrane using KSM-17 | |
JP5817977B2 (en) | Method for producing technetium-99m solution having high concentration and high radioactivity | |
CN101468791B (en) | Extraction and purification technique for producing iodine-131 using homogeneous solution-type reactor | |
CN103301652B (en) | Separation device for gallium-containing radioactive solution | |
Matsumura et al. | Separation of trivalent minor actinides from fission products using single R-BTP column extraction chromatography | |
WO2010001728A1 (en) | Method for separating radioactive copper using chelate exchange resin | |
CN211455322U (en) | Actinium-225 nuclide purifying device | |
TWI451444B (en) | Germanium -68 / gallium-68 radioactive nuclear species generator device | |
CN113509750A (en) | Molybdenum-technetium separation column and molybdenum-technetium separation method | |
US7214318B2 (en) | Method for separation of actinide elements | |
Mani | Reactor production of radionuclides for generators | |
CN111500861B (en) | Method for extracting technetium from neutral molybdenum solution by using activated carbon fiber | |
CN113509838A (en) | Molybdenum-technetium separation device and separation method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |