CN108404667B - A method for centrifuging carbon isotopes with iodomethane as a medium - Google Patents
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 43
- INQOMBQAUSQDDS-UHFFFAOYSA-N iodomethane Chemical compound IC INQOMBQAUSQDDS-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title claims abstract description 21
- OKJPEAGHQZHRQV-UHFFFAOYSA-N Triiodomethane Natural products IC(I)I OKJPEAGHQZHRQV-UHFFFAOYSA-N 0.000 title 1
- 239000000463 material Substances 0.000 claims abstract description 80
- 239000007789 gas Substances 0.000 claims abstract description 52
- 238000000926 separation method Methods 0.000 claims abstract description 44
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000009826 distribution Methods 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 239000012535 impurity Substances 0.000 claims abstract description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 9
- 239000002994 raw material Substances 0.000 claims abstract description 9
- 239000000126 substance Substances 0.000 claims abstract description 8
- 239000012530 fluid Substances 0.000 claims abstract description 7
- 238000004949 mass spectrometry Methods 0.000 claims description 6
- 238000004458 analytical method Methods 0.000 claims description 5
- 239000012141 concentrate Substances 0.000 claims description 4
- 238000000746 purification Methods 0.000 claims description 2
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000005119 centrifugation Methods 0.000 description 8
- 238000005372 isotope separation Methods 0.000 description 6
- OKTJSMMVPCPJKN-OUBTZVSYSA-N Carbon-13 Chemical compound [13C] OKTJSMMVPCPJKN-OUBTZVSYSA-N 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 150000002500 ions Chemical class 0.000 description 4
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-IGMARMGPSA-N Carbon-12 Chemical compound [12C] OKTJSMMVPCPJKN-IGMARMGPSA-N 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000004202 carbamide Substances 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052740 iodine Inorganic materials 0.000 description 2
- 239000011630 iodine Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- YZCKVEUIGOORGS-OUBTZVSYSA-N Deuterium Chemical compound [2H] YZCKVEUIGOORGS-OUBTZVSYSA-N 0.000 description 1
- 241000590002 Helicobacter pylori Species 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000003759 clinical diagnosis Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000012938 design process Methods 0.000 description 1
- 229910052805 deuterium Inorganic materials 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000003745 diagnosis Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000036267 drug metabolism Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229940037467 helicobacter pylori Drugs 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- ZCYVEMRRCGMTRW-IGMARMGPSA-N iodine-127 atom Chemical compound [127I] ZCYVEMRRCGMTRW-IGMARMGPSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D59/00—Separation of different isotopes of the same chemical element
- B01D59/20—Separation by centrifuging
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- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
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Abstract
一种以碘甲烷为介质离心分离碳同位素的方法,包括:净化碘甲烷原料中的轻杂质,使其化学纯度达到碘甲烷的离心分离要求;将净化后的气态碘甲烷通入气体离心机,调节供料流量、以及气体离心机的精料管口和贫料管口的压强,从精料管口和贫料管口分别分离出精料和贫料;维持碘甲烷供料和精料、贫料的流体参数稳定,待气体离心机连续运行至其内碳同位素丰度分布稳定后,通过液氮冷阱分别收集碳同位素丰度分布稳定的精料和贫料。本发明的方法能耗低,分离系数较大,工作介质可以视为没有碳元素以外的同位素干扰,适用于级联形式的规模化生产。
A method for centrifugal separation of carbon isotopes using methyl iodide as a medium, comprising: purifying light impurities in the raw material of methyl iodide so that its chemical purity meets the requirements for centrifugal separation of methyl iodide; passing the purified gaseous methyl iodide into a gas centrifuge, Adjust the feed flow rate and the pressure of the fine material nozzle and the lean material nozzle of the gas centrifuge to separate the fine material and the lean material from the fine material nozzle and the lean material nozzle respectively; maintain the supply of methyl iodide and the fine material, The fluid parameters of the lean material are stable. After the gas centrifuge runs continuously until the carbon isotope abundance distribution in it is stable, the fine material and the lean material with stable carbon isotope abundance distribution are collected respectively through the liquid nitrogen cold trap. The method of the invention has low energy consumption and large separation coefficient, and the working medium can be regarded as having no isotope interference other than carbon elements, and is suitable for large-scale production in the form of cascading.
Description
技术领域technical field
本发明涉及同位素分离制备技术领域,特别涉及一种以碘甲烷为介质离心分离碳同位素的方法。The invention relates to the technical field of isotope separation and preparation, in particular to a method for centrifugally separating carbon isotopes using methyl iodide as a medium.
背景技术Background technique
碳有两种天然稳定同位素:碳-12(98.9%)、碳-13(1.1%)。近些年来碳-13在农业生态、药物代谢、医疗诊断等方面的应用越来越广泛,尤其是富集碳-13尿素呼气试验(UreaBreath Test,简称UBT)已经成为幽门螺杆菌临床诊断的主要手段。富集碳-13尿素呼气试验的国内市场处于增长阶段,且有发展潜力优势,因此经济、高效的碳同位素分离制备方法越来越受到关注。Carbon has two natural stable isotopes: carbon-12 (98.9%) and carbon-13 (1.1%). In recent years, carbon-13 has been widely used in agricultural ecology, drug metabolism, medical diagnosis, etc., especially the carbon-13-enriched urea breath test (UBT) has become the standard for clinical diagnosis of Helicobacter pylori. primary means. The domestic market of carbon-13-enriched urea breath test is in the growth stage, and has the advantages of development potential. Therefore, economical and efficient carbon isotope separation and preparation methods are attracting more and more attention.
气体离心法的原理是利用气体离心机的离心力场中,不同相对分子质量的组分形成的径向压强分布不同,从而实现各组分之间的相对分离,而非同位素之间的绝对分开。通过分离单元的并联和串联,构成离心分离级联,可以获得高丰度产品。气体离心机的结构为一股供料、两股出料,其中轻组分在精料端富集,重组分在贫料端富集。气体离心分离效果受多方面影响,包括工作介质的物性参数、离心机结构参数、离心分离流体参数等影响,由于气体离心机应用于铀浓缩生产的特殊性,部分性能参数处于保密状态。The principle of gas centrifugation is to use the centrifugal force field of the gas centrifuge to form different radial pressure distributions of components with different relative molecular masses, so as to realize the relative separation between components, rather than the absolute separation between isotopes. Through the parallel connection and series connection of separation units, a centrifuge separation cascade is formed, and high-abundance products can be obtained. The structure of the gas centrifuge is one feed and two discharges, in which the light components are enriched at the fine material end, and the heavy components are enriched at the lean material end. The effect of gas centrifugation is affected by many aspects, including the physical parameters of the working medium, the structural parameters of the centrifuge, and the parameters of the centrifuge fluid. Due to the particularity of the application of gas centrifuges in uranium enrichment production, some performance parameters are kept secret.
碳同位素的分离制备方法主要有低温精馏法、化学交换法、气体离心法等,其中低温精馏法在国外已形成工业化生产,国际上富集碳-13的生产能力可达到700kg/a,主要产地是美国。国内碳同位素的分离制备研究也已开展多年,上海化工研究院正致力于低温精馏法的工业化;清华大学工程物理系先后以正辛烷和氟利昂-11为工作介质实现了碳同位素的气体离心分离。除此之外,未见国内外其他有关碳同位素分离制备方法的公开文献发表。但上述碳同位素的气体离心分离方法,均存在需要多元分离的问题,且分离系数相对较小,在用于级联生产时,会带来更高的设备成本,级联设计工艺也更为复杂。The separation and preparation methods of carbon isotopes mainly include cryogenic rectification, chemical exchange, gas centrifugation, etc. Among them, cryogenic rectification has been industrialized abroad, and the production capacity of carbon-13 enrichment in the world can reach 700kg/a. The main place of origin is the United States. Domestic research on the separation and preparation of carbon isotopes has also been carried out for many years. The Shanghai Research Institute of Chemical Industry is committed to the industrialization of cryogenic distillation; the Department of Engineering Physics of Tsinghua University has successively realized the gas centrifugation of carbon isotopes using n-octane and Freon-11 as working media. separate. In addition, there are no other published literatures about carbon isotope separation and preparation methods at home and abroad. However, the gas centrifugal separation methods of carbon isotopes mentioned above all have the problem of multi-component separation, and the separation coefficient is relatively small. When used in cascade production, it will bring higher equipment costs, and the cascade design process is also more complicated. .
发明内容Contents of the invention
有鉴于此,本发明的主要目的在于提供一种以碘甲烷为介质离心分离碳同位素的方法,以期至少部分地解决上述提及的技术问题中的至少之一。In view of this, the main purpose of the present invention is to provide a method for centrifugal separation of carbon isotopes using methyl iodide as a medium, in order to at least partially solve at least one of the above-mentioned technical problems.
为实现上述目的,本发明的技术方案如下:To achieve the above object, the technical scheme of the present invention is as follows:
一种以碘甲烷为介质离心分离碳同位素的方法,包括:A method for centrifugal separation of carbon isotopes using methyl iodide as a medium, comprising:
步骤A:净化碘甲烷原料中的轻杂质,使其化学纯度达到碘甲烷的离心分离要求;Step A: purify the light impurities in the raw material of methyl iodide, so that its chemical purity meets the centrifugal separation requirements of methyl iodide;
步骤B:将净化后的气态碘甲烷通入气体离心机,调节供料流量、以及气体离心机的精料管口和贫料管口的压强,从所述精料管口和贫料管口分别分离出精料和贫料;Step B: Pass the purified gaseous methyl iodide into the gas centrifuge, adjust the feed flow rate, and the pressure of the fine material nozzle and the lean material nozzle of the gas centrifuge, from the fine material nozzle and the lean material nozzle Separation of fine material and lean material;
步骤C:维持碘甲烷供料和精料、贫料的流体参数稳定,待所述气体离心机连续运行至其内碳同位素丰度分布稳定后,通过液氮冷阱分别收集碳同位素丰度分布稳定的所述精料和贫料。Step C: Keep the fluid parameters of methyl iodide feed, concentrate, and lean material stable, and after the gas centrifuge runs continuously until the carbon isotope abundance distribution in it is stable, collect the carbon isotope abundance distribution respectively through a liquid nitrogen cold trap Stable concentrate and lean feed.
优选地,步骤A中,所述碘甲烷原料净化后化学纯度达到99.5%以上。Preferably, in step A, the chemical purity of the methyl iodide raw material reaches above 99.5% after purification.
优选地,步骤B中,所述气体离心机的供料流量为11.5~19.5g/h,分流比为0.4~0.6,所述气体离心机的精料管口、贫料管口的压强均为175~300Pa。Preferably, in step B, the feed flow rate of the gas centrifuge is 11.5 to 19.5 g/h, the split ratio is 0.4 to 0.6, and the pressures of the fine material nozzle and the lean material nozzle of the gas centrifuge are both 175~300Pa.
优选地,步骤C中,使气体离心机连续运行1.5小时以上,以使其内碳同位素丰度分布稳定。Preferably, in step C, the gas centrifuge is operated continuously for more than 1.5 hours, so as to stabilize the carbon isotope abundance distribution in it.
优选地,步骤C中,还包括对所述精料和贫料进行质谱分析以获取分离系数的步骤:调节所述气体质谱仪的离子源参数,以(CH3I)+离子团为分析对象,从而对精料、贫料的碳同位素含量进行准确分析,以计算分离系统。Preferably, in step C, it also includes the step of performing mass spectrometry analysis on the fine material and the lean material to obtain the separation coefficient: adjust the ion source parameters of the gas mass spectrometer, and use (CH 3 I) + ion groups as the analysis object , so as to accurately analyze the carbon isotope content of fine material and lean material to calculate the separation system.
优选地,所述气体离心机为单机或级联机。Preferably, the gas centrifuge is a single machine or a cascade machine.
基于上述技术方案,本发明的有益效果如下:Based on the above-mentioned technical scheme, the beneficial effects of the present invention are as follows:
(1)本发明以碘甲烷为工作介质,可视为没有碳元素以外的同位素干扰避免了复杂的多元分离问题,在离心分离生产级联设计及优化方面具有优势,具备较强的技术可行性以及一定的经济性。(1) The present invention uses methyl iodide as the working medium, which can be regarded as having no isotope interference other than carbon elements and avoiding complex multi-component separation problems. It has advantages in cascade design and optimization of centrifugal separation production, and has strong technical feasibility and a certain economy.
(2)以碘甲烷为工作介质,通过合理调整气体离心机的工作参数如压强、流量等,单机分离系数达到1.11,适用于级联形式的规模化生产,并且得到的贫料与原料只是在丰度上有所差异,完全不影响其作为化学试剂回收继续使用,因此该方法的市场应用价值具有一定优势。(2) Using methyl iodide as the working medium, by reasonably adjusting the working parameters of the gas centrifuge such as pressure and flow, the separation coefficient of the single machine can reach 1.11, which is suitable for large-scale production in the form of cascading, and the obtained lean material and raw material are only in the The difference in abundance does not affect its continuous use as a chemical reagent recovery, so the market application value of this method has certain advantages.
(3)本发明的碳同位素分离方法相比于目前碳同位素的工业化生产方法,即低温精馏法,能耗更低。(3) The carbon isotope separation method of the present invention has lower energy consumption than the current industrialized production method of carbon isotope, that is, cryogenic distillation.
附图说明Description of drawings
图1为本发明实施例以碘甲烷为介质离心分离碳同位素的系统结构示意图;Fig. 1 is a schematic diagram of the system structure of an embodiment of the present invention using methyl iodide as a medium for centrifuging carbon isotopes;
图2为本发明实施例以碘甲烷为介质离心分离碳同位素的方法流程图;Fig. 2 is the method flowchart of the embodiment of the present invention using methyl iodide as a medium for centrifuging carbon isotopes;
图3为本发明实施例1采用单机分离碘甲烷的质谱分析结果。Fig. 3 is the result of mass spectrometry analysis of the separation of methyl iodide by a single machine in Example 1 of the present invention.
上述附图中,附图标记含义具体如下:In the above drawings, the meanings of reference signs are as follows:
1-气体离心机;2-贫料罐;3-精料罐;4-液氮冷阱;5-取样器;6-气体质谱仪;7-真空泵。1-gas centrifuge; 2-lean material tank; 3-fine material tank; 4-liquid nitrogen cold trap; 5-sampler; 6-gas mass spectrometer; 7-vacuum pump.
具体实施方式Detailed ways
为使本发明的目的、技术方案和优点更加清楚明白,以下结合具体实施例,并参照附图,对本发明作进一步的详细说明。In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with specific embodiments and with reference to the accompanying drawings.
对于气体离心法分离碳同位素,工作介质是关键要素之一,气体离心法的工作介质一般应满足以下三个条件:For the separation of carbon isotopes by gas centrifugation, the working medium is one of the key elements. The working medium of gas centrifugation should generally meet the following three conditions:
1)在低于300℃的温度条件下保持稳定,不分解;1) It remains stable at temperatures below 300°C and does not decompose;
2)相对分子质量不小于70;2) The relative molecular mass is not less than 70;
3)常温下,饱和蒸气压不小于665Pa。3) At room temperature, the saturated vapor pressure is not less than 665Pa.
碘甲烷(CH3I)相对分子质量为141.94,难热解,室温下的饱和蒸气压约为50kPa,满足气体离心法对工作介质的要求,同时碘甲烷作为常见的化学试剂,其制取具有稳定而成熟的工艺,这也是选择其作为工作介质的优势条件。Methyl iodide (CH 3 I ) has a relative molecular mass of 141.94, is difficult to pyrolyze, and has a saturated vapor pressure of about 50kPa at room temperature, meeting the requirements of gas centrifugation for the working medium. Stable and mature technology, which is also the advantage of choosing it as a working medium.
本发明提出以碘甲烷为介质离心分离碳同位素的方法,由于碘的天然稳定同位素只有碘-127一种,而氢的同位素氘天然丰度极低(0.0115%),完全可以视工作介质碘甲烷为二元分离,两种组分分别为12CH3I和13CH3I,对应的相对分子质量为142和143,避免引入多元分离的问题,同时也达到了很好的碳同位素分离效果。The present invention proposes a method for centrifuging carbon isotopes with methyl iodide as a medium. Since the natural stable isotope of iodine is only iodine-127, and the natural abundance of deuterium isotope of hydrogen is extremely low (0.0115%), it can be completely determined by the working medium methyl iodide For binary separation, the two components are 12 CH 3 I and 13 CH 3 I, respectively, and the corresponding relative molecular masses are 142 and 143, which avoids the problem of introducing multi-component separation, and also achieves a good carbon isotope separation effect.
该方法可利用已有的气体离心分离系统实现,该气体离心分离系统结构如图1所示,包括气体离心机1、供取料单元、贫料罐2、精料罐3、液氮冷阱4、取料器5和真空泵7,其中:This method can be realized by using the existing gas centrifugal separation system. The structure of the gas centrifugal separation system is shown in Figure 1, including a gas centrifuge 1, a feeding and retrieving unit, a lean material tank 2, a fine material tank 3, and a liquid nitrogen cold trap 4. Reclaimer 5 and vacuum pump 7, wherein:
气体离心机1的结构为本技术领域内常规结构,通过供取料单元向气体分离机1输送碘甲烷以进行碳同位素分离,经气体分离机1分离出的贫料、精料分别通过供取料单元输送至贫料罐2和精料罐3内,贫料罐2和精料罐3设置于液氮冷阱4内,以对精料和贫料进行冷却收集,真空泵7连接至供取料单元,以维持供取料单元的空气分压在一定范围内。The structure of the gas centrifuge 1 is a conventional structure in this technical field. The methyl iodide is delivered to the gas separator 1 through the supply and take-off unit for carbon isotope separation. The material unit is transported to the lean material tank 2 and the fine material tank 3. The lean material tank 2 and the fine material tank 3 are set in the liquid nitrogen cold trap 4 to cool and collect the fine material and the lean material. The vacuum pump 7 is connected to the supply and extraction The material unit is used to maintain the air partial pressure of the supply and reclaim unit within a certain range.
图2为本发明实施例以碘甲烷为介质离心分离碳同位素的方法流程图。如图2本发明提供一种以碘甲烷为介质离心分离碳同位素的方法,包括:Fig. 2 is a flowchart of a method for centrifuging carbon isotopes using methyl iodide as a medium according to an embodiment of the present invention. As shown in Figure 2, the present invention provides a method for centrifuging carbon isotopes with methyl iodide as a medium, including:
步骤A:净化碘甲烷原料中的轻杂质,使其化学纯度达到碘甲烷的离心分离要求;Step A: purify the light impurities in the raw material of methyl iodide, so that its chemical purity meets the centrifugal separation requirements of methyl iodide;
其中,轻杂质为本领域中专业术语,是指相对于工作介质的分子量小很多的杂质,例如分子量为工作介质分子量的50%以下的杂质;此处的轻杂质即为相对于碘甲烷原料分子量小很多的杂质,主要是空气及水蒸气,对于天然碘甲烷原料,即天然丰度下的碘甲烷原料,可以以液氮和“液氮-无水乙醇”混合物为冷却剂,利用碘甲烷与轻杂质饱和蒸气压的差异进行净化,使其化学纯度达到99.5%以上,以满足进行气体离心分离的要求。Wherein, light impurity is a professional term in this field, refers to the impurity that the molecular weight of relative to working medium is much smaller, for example molecular weight is the impurity below 50% of working medium molecular weight; Much smaller impurities are mainly air and water vapor. For natural methyl iodide raw materials, that is, methyl iodide raw materials in natural abundance, liquid nitrogen and "liquid nitrogen-absolute ethanol" mixtures can be used as coolants, using methyl iodide and methyl iodide The difference in saturated vapor pressure of light impurities is purified to make its chemical purity reach more than 99.5%, so as to meet the requirements of gas centrifugal separation.
步骤B:将净化后的气态碘甲烷通入气体离心机,调节供料流量、以及气体离心机的精料管口和贫料管口的压强,从所述精料管口和贫料管口分别分离出精料和贫料;Step B: Pass the purified gaseous methyl iodide into the gas centrifuge, adjust the feed flow rate, and the pressure of the fine material nozzle and the lean material nozzle of the gas centrifuge, from the fine material nozzle and the lean material nozzle Separation of fine material and lean material;
作为示例,本发明所使用的气体离心机1为单机形式的气体离心机,供取料单元内设置有供料孔板,通过管道连接至气体离心机1,可通过该供料孔板调节碘甲烷以11.5~19.5g/h的供料流量通入气体离心机1;在供取料单元与气体离心机连接的管道上还设置有阀门,通过阀门调节分流比为0.4~0.6,精料管口和贫料管口的压强为175~300Pa,在该条件下可保证碳同位素的较高分离系数。As an example, the gas centrifuge 1 used in the present invention is a gas centrifuge in stand-alone form, and a feeding orifice is arranged in the feeding and reclaiming unit, which is connected to the gas centrifuge 1 through a pipeline, and iodine can be adjusted through the feeding orifice. Methane is fed into the gas centrifuge 1 at a feed flow rate of 11.5-19.5g/h; a valve is also installed on the pipeline connecting the supply and take-off unit with the gas centrifuge, and the split ratio is adjusted to 0.4-0.6 through the valve. The pressure at the outlet and the lean material nozzle is 175-300Pa, under which conditions a higher separation factor of carbon isotopes can be guaranteed.
在分离过程中,通过真空泵7维持供取料单元的空气分压在2Pa以内,通过液氮冷阱分别收集精料和贫料。During the separation process, the vacuum pump 7 is used to maintain the air partial pressure of the feeding and retrieving unit within 2 Pa, and the fine material and lean material are collected respectively through a liquid nitrogen cold trap.
步骤C:维持碘甲烷供料和精料、贫料的流体参数稳定,待所述气体离心机连续运行至碳同位素丰度分布稳定后,得到含浓缩/贫化的碳同位素的精料和贫料。Step C: Maintain the stability of the fluid parameters of methyl iodide feedstock, fine material, and lean material. After the gas centrifuge continues to run until the carbon isotope abundance distribution is stable, obtain concentrated/depleted carbon isotope-containing fine material and lean material. material.
作为优选,应当待碘甲烷供料和精料、贫料的流体参数达到稳定后,使气体离心机运行1.5小时以上,以使其内碳同位素分度分布稳定;As preferably, after the fluid parameters of methyl iodide supply and concentrated material and lean material are stabilized, the gas centrifuge is operated for more than 1.5 hours, so that the carbon isotope distribution in it is stable;
本步骤中还包括对所述精料和贫料取样并使用气体质谱仪进行质谱分析的步骤,以计算分离系数。其中,对所述精料和贫料进行质谱分析的步骤包括:调节所述气体质谱仪的离子源参数,以(CH3I)+离子团为分析对象,从而对精料、贫料的碳同位素含量进行准确分析。This step also includes the step of sampling the fine material and the lean material and using a gas mass spectrometer for mass spectrometry analysis to calculate the separation factor. Wherein, the step of performing mass spectrometry analysis on the fine material and lean material includes: adjusting the ion source parameters of the gas mass spectrometer, using (CH 3 I) + ion groups as the analysis object, so as to analyze the carbon content of the fine material and lean material. Accurate analysis of isotope content.
以下列举具体实施例对本发明的技术方案作进一步说明:Below enumerate specific embodiment technical scheme of the present invention is further described:
实施例1Example 1
通过调节供料孔板,将净化后的气态碘甲烷以15g/h左右的供料流量通入单机形式的气体离心机,通过供取料单元的阀门调节离心机精、贫料管口压强在230Pa左右,分流比为0.5,待碘甲烷供料和精料、贫料的流体参数均达到稳定状态后,气体离心机须连续稳定运行1.5小时以上,然后同时分别在精料罐、贫料罐处使用液氮冷阱收料,分离过程中使用真空泵维持供取料单元空气分压在2Pa以内。By adjusting the feeding orifice, the purified gaseous methyl iodide is fed into the single-machine gas centrifuge at a feeding flow rate of about 15g/h, and the pressure of the fine and lean material nozzles of the centrifuge is adjusted through the valve of the feeding and retrieving unit. At about 230Pa, the split ratio is 0.5. After the fluid parameters of the methyl iodide supply and the fine material and lean material reach a steady state, the gas centrifuge must run continuously and stably for more than 1.5 hours, and then simultaneously separate the fine material tank and the lean material tank. A liquid nitrogen cold trap is used to collect materials, and a vacuum pump is used to maintain the air partial pressure of the feeding and reclaiming unit within 2Pa during the separation process.
通过样品分析得到分离系数,其计算公式为:γ=[Cp/(1-Cp)]/[Cw/(1-Cw)],其中γ为分离系数,Cp为精料中碳-12的丰度,Cw为贫料中碳-12的丰度。本实施例的单机离心分离的结果如图3所示,根据质谱分析的结果计算得到单机分离系数为1.11。现有技术中以正辛烷为介质分离碳同位素的单机分离系数为1.08,以氟利昂为介质分离碳同位素的单机分离系数为1.08,相较而言,本发明以碘甲烷为介质离心分离碳同位素的方法的有效性,适用于级联形式的规模化生产。The separation coefficient is obtained through sample analysis, and its calculation formula is: γ=[C p /(1-C p )]/[C w /(1-C w )], where γ is the separation coefficient, and C p is the The abundance of carbon-12, Cw is the abundance of carbon-12 in the lean material. The results of the centrifugation of the single machine in this embodiment are shown in FIG. 3 , and the separation coefficient of the single machine was calculated to be 1.11 according to the results of the mass spectrometry analysis. In the prior art, the single-machine separation coefficient for separating carbon isotopes with n-octane as a medium is 1.08, and the single-machine separation coefficient for separating carbon isotopes with Freon as a medium is 1.08. In comparison, the present invention uses methyl iodide as a medium for centrifugal separation of carbon isotopes The effectiveness of the method is suitable for large-scale production in cascaded form.
以上所述的具体实施例,对本发明的目的、技术方案和有益效果进行了进一步详细说明,应理解的是,以上所述仅为本发明的具体实施例而已,并不用于限制本发明,凡在本发明的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The specific embodiments described above have further described the purpose, technical solutions and beneficial effects of the present invention in detail. It should be understood that the above descriptions are only specific embodiments of the present invention, and are not intended to limit the present invention. Within the spirit and principles of the present invention, any modifications, equivalent replacements, improvements, etc., shall be included in the protection scope of the present invention.
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