CN116062708B - Synthetic method of sodium thiosulfate - Google Patents
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- CN116062708B CN116062708B CN202211534587.5A CN202211534587A CN116062708B CN 116062708 B CN116062708 B CN 116062708B CN 202211534587 A CN202211534587 A CN 202211534587A CN 116062708 B CN116062708 B CN 116062708B
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- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 title claims abstract description 21
- 235000019345 sodium thiosulphate Nutrition 0.000 title claims abstract description 21
- 238000010189 synthetic method Methods 0.000 title abstract description 4
- 238000006243 chemical reaction Methods 0.000 claims abstract description 35
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000011593 sulfur Substances 0.000 claims abstract description 34
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 34
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 229940101006 anhydrous sodium sulfite Drugs 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 13
- 239000013078 crystal Substances 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 11
- 239000000126 substance Substances 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims description 15
- 229910052979 sodium sulfide Inorganic materials 0.000 claims description 9
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 claims description 9
- 230000002194 synthesizing effect Effects 0.000 claims description 6
- 125000004434 sulfur atom Chemical group 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000005338 heat storage Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 2
- 238000004042 decolorization Methods 0.000 abstract 1
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 230000036632 reaction speed Effects 0.000 abstract 1
- 238000007670 refining Methods 0.000 abstract 1
- 239000011734 sodium Substances 0.000 description 34
- 239000000047 product Substances 0.000 description 10
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000002441 X-ray diffraction Methods 0.000 description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 6
- 229940001482 sodium sulfite Drugs 0.000 description 6
- 235000010265 sodium sulphite Nutrition 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- 238000000634 powder X-ray diffraction Methods 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- PODWXQQNRWNDGD-UHFFFAOYSA-L sodium thiosulfate pentahydrate Chemical compound O.O.O.O.O.[Na+].[Na+].[O-]S([S-])(=O)=O PODWXQQNRWNDGD-UHFFFAOYSA-L 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000011232 storage material Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 2
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 2
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 241000779819 Syncarpia glomulifera Species 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 208000012839 conversion disease Diseases 0.000 description 1
- 230000000382 dechlorinating effect Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000005580 one pot reaction Methods 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 239000001739 pinus spp. Substances 0.000 description 1
- 238000004445 quantitative analysis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- HYHCSLBZRBJJCH-UHFFFAOYSA-N sodium polysulfide Chemical compound [Na+].S HYHCSLBZRBJJCH-UHFFFAOYSA-N 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 229940036248 turpentine Drugs 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/64—Thiosulfates; Dithionites; Polythionates
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
技术领域Technical Field
本发明属于合成化学领域,具体涉及一种硫代硫酸钠的绿色化学合成方法。The invention belongs to the field of synthetic chemistry, and in particular relates to a green chemical synthesis method of sodium thiosulfate.
背景技术Background Art
硫代硫酸钠俗称“海波”,又名“大苏打”,是无色透明晶体;易溶于水,也易溶于氨水和松节油,难溶于乙醇。它在酸性条件下不稳定,易分解;在有机化学中能用作硫源,用于生产含硫化合物;具有较强的还原性和配位能力,可用作照相行业的定影剂,洗染和造纸业的脱氯剂,定量分析中的还原剂,医药上的洗涤剂和消毒剂;它在48℃发生相变,能溶于其结晶水中,能吸收大量的热,达到210J/g,能用作大规模储热材料。Sodium thiosulfate, commonly known as "Haibo" or "baking soda", is a colorless transparent crystal. It is easily soluble in water, ammonia and turpentine, but difficult to dissolve in ethanol. It is unstable under acidic conditions and easily decomposes. It can be used as a sulfur source in organic chemistry to produce sulfur-containing compounds. It has strong reducing and coordination abilities and can be used as a fixer in the photographic industry, a dechlorinating agent in the laundry and papermaking industries, a reducing agent in quantitative analysis, and a detergent and disinfectant in medicine. It undergoes a phase change at 48°C, can dissolve in its crystal water, can absorb a large amount of heat, up to 210 J/g, and can be used as a large-scale heat storage material.
现有技术中,硫代硫酸钠是在水溶液中制备的。可用的方法有二:(1)亚硫酸钠和硫磺在沸腾的水溶液中经数小时的反应,然后过滤除去未反应的硫磺,再经浓缩、结晶得到五水硫代硫酸钠;(2)使用硫化钠、碳酸钠和二氧化硫反应制备。这两种工艺的差异在于后者硫磺由二氧化硫(或亚硫酸钠——二氧化硫与碳酸钠的反应产物)与硫化钠反应原位产生。两种方法步骤多,最大的缺点在于反应不完全、溶剂用量大,最后需要经过过滤、浓缩结晶得到产物。方法二还需要制造具有强烈刺激性的SO2,Na2S因为水解会产生恶臭的H2S,因此能耗高,对环境不友好。In the prior art, sodium thiosulfate is prepared in an aqueous solution. There are two available methods: (1) sodium sulfite and sulfur react in a boiling aqueous solution for several hours, then filter out the unreacted sulfur, and then concentrate and crystallize to obtain sodium thiosulfate pentahydrate; (2) sodium sulfide, sodium carbonate and sulfur dioxide are used to react. The difference between the two processes is that the sulfur in the latter is produced in situ by the reaction of sulfur dioxide (or sodium sulfite - the reaction product of sulfur dioxide and sodium carbonate) with sodium sulfide. Both methods have many steps, and the biggest disadvantage is that the reaction is incomplete and the amount of solvent used is large. Finally, the product needs to be filtered, concentrated and crystallized. Method 2 also requires the production of highly irritating SO2 , and Na2S produces malodorous H2S due to hydrolysis, so it consumes a lot of energy and is not environmentally friendly.
发明内容Summary of the invention
发明目的:本发明的目的是提供一种反应完全、绿色环保和高效的硫代硫酸钠的合成方法。Purpose of the invention: The purpose of the present invention is to provide a method for synthesizing sodium thiosulfate which is completely reactive, environmentally friendly and efficient.
技术方案:本发明公开了一种硫代硫酸钠的合成方法,包括以下步骤:按照硫磺、无水亚硫酸钠和水摩尔比1:0.95~1.05:5~10取各物质,加入搅拌反应器进行反应,控制反应温度为100~120℃,反应结束后将所得液体冷却,即得到硫代硫酸钠结晶,其中,所述硫磺的摩尔质量以硫原子计。Technical solution: The present invention discloses a method for synthesizing sodium thiosulfate, comprising the following steps: taking various substances according to a molar ratio of sulfur, anhydrous sodium sulfite and water of 1:0.95-1.05:5-10, adding them into a stirred reactor for reaction, controlling the reaction temperature to be 100-120°C, cooling the obtained liquid after the reaction is completed, and obtaining sodium thiosulfate crystals, wherein the molar mass of the sulfur is calculated in terms of sulfur atoms.
优选的,按照硫磺、无水亚硫酸钠和水摩尔比1:1:5取各物质,控制反应温度为115~120℃。Preferably, sulfur, anhydrous sodium sulfite and water are prepared in a molar ratio of 1:1:5, and the reaction temperature is controlled at 115-120°C.
进一步优选的,所述反应温度为115℃。More preferably, the reaction temperature is 115°C.
优选的,所述搅拌反应器搅拌速度为200~400rpm。Preferably, the stirring speed of the stirred reactor is 200 to 400 rpm.
优选的,按照无水亚硫酸钠摩尔数的1%~5%加入催化剂。Preferably, the catalyst is added at 1% to 5% of the molar amount of anhydrous sodium sulfite.
优选的,所述催化剂为碱性物质。Preferably, the catalyst is an alkaline substance.
进一步优选的,所述催化剂为NaOH、Na2CO3、Na2S中的至少一种。More preferably, the catalyst is at least one of NaOH, Na 2 CO 3 and Na 2 S.
优选的,所述反应时间为2~6h。Preferably, the reaction time is 2 to 6 hours.
从化学原理上看,硫代硫酸钠的合成反应如下:From a chemical perspective, the synthesis reaction of sodium thiosulfate is as follows:
1/8S8+Na2SO3+5H2O=Na2S2O3·5H2O1/8S 8 +Na 2 SO 3 +5H 2 O=Na 2 S 2 O 3 ·5H 2 O
当反应物硫磺、亚硫酸钠和水的摩尔比按照反应计量摩尔比S:Na2SO3:H2O=1:0.95~1.05:5~10投料时,水既是反应物又是反应的溶剂,在所述条件下得到的液体产物在降温后变为固体Na2S2O3·5H2O,可以不经提纯直接用作储热材料,具有无比的优越性。因为硫磺是石油、天然气脱硫产物,亚硫酸钠是能源工业(热电、供热)脱除SO2的产物,也可以作为硫磺和亚硫酸钠的高值利用手段。When the molar ratio of the reactants sulfur, sodium sulfite and water is fed according to the reaction stoichiometric molar ratio S:Na 2 SO 3 :H 2 O=1:0.95-1.05:5-10, water is both a reactant and a solvent for the reaction. The liquid product obtained under the above conditions becomes solid Na 2 S 2 O 3 ·5H 2 O after cooling, which can be directly used as a heat storage material without purification, and has unparalleled advantages. Because sulfur is a product of desulfurization of petroleum and natural gas, and sodium sulfite is a product of removing SO 2 in the energy industry (thermal power, heating), it can also be used as a high-value utilization method of sulfur and sodium sulfite.
有益效果:与现有技术相比,本发明具有如下显著优点:Beneficial effects: Compared with the prior art, the present invention has the following significant advantages:
1、本发明提供的合成方法按照反应计量摩尔比S:Na2SO3:H2O=1:0.95~1.05:5~10投料时,反应物和产物在反应过程中长时间以固体形式存在,反应完全;特别是当反应物按照计量摩尔比S:Na2SO3:H2O=1:1:5投料时,反应结束后无需蒸发过滤即全部转化为Na2S2O3·5H2O,是原子经济性100%的反应,单位容器产能达到最大。1. When the synthetic method provided by the present invention feeds materials according to the reaction stoichiometric molar ratio S:Na 2 SO 3 :H 2 O=1:0.95-1.05:5-10, the reactants and products exist in solid form for a long time during the reaction process, and the reaction is complete; in particular, when the reactants are fed according to the stoichiometric molar ratio S:Na 2 SO 3 :H 2 O=1:1:5, after the reaction is completed, all of them are converted into Na 2 S 2 O 3 ·5H 2 O without evaporation and filtration, which is a reaction with 100% atomic economy and the production capacity per unit container reaches the maximum.
2、本方法投入的水转化为Na2S2O3·5H2O中的结晶水,反应使用的溶剂量被减到了最少,有利于反应的进行。2. The water input in this method is converted into crystal water in Na 2 S 2 O 3 ·5H 2 O, and the amount of solvent used in the reaction is reduced to a minimum, which is beneficial to the reaction.
3、本发明所需生产设备为常见的搅拌反应器,反应一步完成,不涉及SO2、H2S等有毒、污染性气体,能耗最低,实现了绿色环保的生产要求,如产品用作储热材料,则不需提纯,可直接销售或使用。3. The production equipment required by the present invention is a common stirring reactor. The reaction is completed in one step, and no toxic and polluting gases such as SO 2 and H 2 S are involved. The energy consumption is minimal, and green and environmentally friendly production requirements are achieved. If the product is used as a heat storage material, it does not need to be purified and can be sold or used directly.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为实施例1合成的Na2S2O3·5H2O的X射线粉末衍射(XRD)图谱。FIG1 is an X-ray powder diffraction (XRD) pattern of Na 2 S 2 O 3 ·5H 2 O synthesized in Example 1. FIG.
图2为实施例2及实施例3下合成的Na2S2O3·5H2O的XRD图谱;其中,A为实施例2所得Na2S2O3·5H2O的XRD图谱,B为实施例3所得Na2S2O3·5H2O的XRD图谱。FIG2 is the XRD patterns of Na 2 S 2 O 3 ·5H 2 O synthesized in Example 2 and Example 3; wherein A is the XRD pattern of Na 2 S 2 O 3 ·5H 2 O obtained in Example 2, and B is the XRD pattern of Na 2 S 2 O 3 ·5H 2 O obtained in Example 3.
具体实施方式DETAILED DESCRIPTION
下面结合具体实施例和附图对本发明的技术方案作进一步说明。The technical solution of the present invention is further described below in conjunction with specific embodiments and drawings.
本发明公开了一种硫代硫酸钠的合成方法,该方法以硫磺、亚硫酸钠和少量的水为原料,在100~120℃的反应温度下,经2~6h的反应,冷却后即得目标产物,是一步完成的原子经济性可达100%的反应,最大程度地节约了生产成本和能耗。The invention discloses a method for synthesizing sodium thiosulfate. The method uses sulfur, sodium sulfite and a small amount of water as raw materials, reacts for 2 to 6 hours at a reaction temperature of 100 to 120 DEG C, and obtains a target product after cooling. The method is a one-step reaction with an atomic economy of up to 100%, thereby saving production costs and energy consumption to the greatest extent.
实施例1Example 1
准确称取硫磺80g(2.5mol S)、无水亚硫酸钠315g(2.5mol)和水225mL(12.5Accurately weigh 80 g sulfur (2.5 mol S), 315 g anhydrous sodium sulfite (2.5 mol) and 225 mL water (12.5
mol)加入搅拌反应器,加热至115℃并控制搅拌速度300rpm反应5h,反应结束后,将所得液体转移至敞口产物槽,冷却后即全部转化为Na2S2O3·5H2O结晶。mol) was added into a stirred reactor, heated to 115°C and stirred at 300 rpm for 5 h. After the reaction, the obtained liquid was transferred to an open product tank and completely converted into Na 2 S 2 O 3 ·5H 2 O crystals after cooling.
实施例2Example 2
准确称取硫磺80g(2.5mol S)、无水亚硫酸钠315g(2.5mol)、水225mL(12.5mol)以及硫化钠0.05mol加入搅拌反应器,在115℃下,控制搅拌速度300rpm反应2.5h。反应结束后,将所得液体转移至敞口产物槽,冷却后得到Na2S2O3·5H2O结晶。Accurately weigh 80 g sulfur (2.5 mol S), 315 g anhydrous sodium sulfite (2.5 mol), 225 mL water (12.5 mol) and 0.05 mol sodium sulfide and add them into a stirred reactor, and react for 2.5 h at 115° C. with a stirring speed of 300 rpm. After the reaction is completed, the resulting liquid is transferred to an open product tank, and Na 2 S 2 O 3 ·5H 2 O crystals are obtained after cooling.
实施例3Example 3
准确称取硫磺80g(2.5mol S)、无水亚硫酸钠315g(2.5mol)、水225mL(12.5mol)以及硫化钠0.1mol加入搅拌反应器,在120℃下,控制搅拌速度250rpm反应2.5h。反应结束后,将所得液体转移至敞口产物槽,冷却后得到Na2S2O3·5H2O结晶。Accurately weigh 80g sulfur (2.5mol S), 315g anhydrous sodium sulfite (2.5mol), 225mL water (12.5mol) and 0.1mol sodium sulfide and add them into a stirred reactor, and react for 2.5h at 120°C with a stirring speed of 250rpm . After the reaction is completed, the obtained liquid is transferred to an open product tank, and Na2S2O3 · 5H2O crystals are obtained after cooling.
实施例4Example 4
准确称取硫磺80g(2.5mol S)、无水亚硫酸钠300g(2.38mol)、水340mL(18.9mol)以及氢氧化钠0.1mol加入搅拌反应器,在100℃搅拌速度250rpm下反应3h。反应结束后,趁热过滤除去未反应的硫磺,然后将所得热溶液立即转移至敞口容器中,冷却后即得到Na2S2O3·5H2O结晶,再次过滤除去残留的溶液,所得到的液体和前面得到的未反应硫磺混合,直接用于下批次合成而循环使用。Accurately weigh 80g sulfur (2.5mol S), 300g anhydrous sodium sulfite (2.38mol), 340mL water (18.9mol) and 0.1mol sodium hydroxide and add them into a stirred reactor, and react for 3h at 100℃ and a stirring speed of 250rpm. After the reaction is completed, filter and remove the unreacted sulfur while hot, and then immediately transfer the obtained hot solution to an open container, and after cooling , obtain Na2S2O3 · 5H2O crystals, and filter and remove the residual solution again, and the obtained liquid is mixed with the unreacted sulfur obtained previously, and directly used for the next batch of synthesis and recycled.
实施例5Example 5
准确称取硫磺80g(2.5mol S)、无水亚硫酸钠330g(2.62mol)、水450mL(25mol)以及碳酸钠0.12mol加入搅拌反应器,在100℃搅拌速度250rpm下反应3h。反应结束后,将所得液体立即转移至敞口容器中,冷却后即得到Na2S2O3·5H2O结晶,过滤除去残留的溶液,所得到的液体可直接用于下批次合成而循环使用。Accurately weigh 80g sulfur (2.5mol S), 330g anhydrous sodium sulfite (2.62mol), 450mL water (25mol) and 0.12mol sodium carbonate into a stirred reactor, and react for 3h at 100℃ and 250rpm . After the reaction, the obtained liquid is immediately transferred to an open container, and after cooling , Na2S2O3 · 5H2O crystals are obtained. The residual solution is filtered to remove the obtained liquid, which can be directly used for the next batch synthesis and recycled.
实施例6Example 6
取实施例1合成的Na2S2O3·5H2O进行X射线衍射实验,使用CuKα辐射。图1为实施例1合成的Na2S2O3·5H2O与标准Na2S2O3·5H2O、Na2S2O3·2H2O、Na2SO3、硫磺的XRD对比图谱。实验结果表明,当反应按照1/8S8+Na2SO3+5H2O=Na2S2O3·5H2O的化学计量比、反应温度为115℃充分搅拌的条件下反应5h进行反应时,耗尽了所有的硫磺,而且液体反应混合物在冷却后完全凝固。Na2S2O3·5H2O是反应的主要产物,还有少量脱水杂质Na2S2O3·2H2O,这可能是由于在反应过程中,部分水从密封不是很严的烧瓶中漏出导致。The Na 2 S 2 O 3 ·5H 2 O synthesized in Example 1 was subjected to an X-ray diffraction experiment using CuKα radiation. FIG1 is a comparative XRD spectrum of the Na 2 S 2 O 3 ·5H 2 O synthesized in Example 1 and standard Na 2 S 2 O 3 ·5H 2 O, Na 2 S 2 O 3 ·2H 2 O, Na 2 SO 3 , and sulfur. The experimental results show that when the reaction is carried out at a stoichiometric ratio of 1/8S 8 +Na 2 SO 3 +5H 2 O=Na 2 S 2 O 3 ·5H 2 O, a reaction temperature of 115°C, and sufficient stirring for 5 hours, all the sulfur is consumed, and the liquid reaction mixture is completely solidified after cooling. Na 2 S 2 O 3 ·5H 2 O is the main product of the reaction, and there is a small amount of dehydrated impurity Na 2 S 2 O 3 ·2H 2 O. This may be due to the fact that during the reaction, some water leaked from the flask which was not sealed tightly.
实施例7Example 7
取实施例2和3合成的Na2S2O3·5H2O进行X射线衍射实验,使用Cu Kα辐射。图2为实施例2(对应图2A)和实施例3(对应图2B)下合成的Na2S2O3·5H2O与标准Na2S2O3·5H2O、Na2S·9H2O、Na2SO3、S8的XRD对比图谱。实验结果表明,X射线衍射图显示只有归于Na2S2O3·5H2O的峰,而没有S8、Na2SO3和Na2S-9H2O的特征衍射峰,可见加入硫化钠可以催化S8和Na2SO3的反应,缩短反应时间。其中,催化剂是通过使硫磺增溶产生作用的。由于硫磺极难溶于水,而且溶解速度极慢,加入碱性物质,可以使硫磺溶解度增加,如硫化钠可以与硫磺反应生成多硫化钠从而起到催化作用。Na 2 S 2 O 3 ·5H 2 O synthesized in Examples 2 and 3 was subjected to X-ray diffraction experiments using Cu Kα radiation. FIG2 is a comparative XRD spectrum of Na 2 S 2 O 3 ·5H 2 O synthesized in Example 2 (corresponding to FIG2A ) and Example 3 (corresponding to FIG2B ) with standard Na 2 S 2 O 3 ·5H 2 O, Na 2 S·9H 2 O, Na 2 SO 3 , and S 8. The experimental results show that the X-ray diffraction pattern shows only peaks attributable to Na 2 S 2 O 3 ·5H 2 O, but no characteristic diffraction peaks of S 8 , Na 2 SO 3 and Na 2 S-9H 2 O. It can be seen that the addition of sodium sulfide can catalyze the reaction of S 8 and Na 2 SO 3 and shorten the reaction time. Among them, the catalyst works by solubilizing sulfur. Since sulfur is extremely insoluble in water and dissolves very slowly, adding alkaline substances can increase the solubility of sulfur. For example, sodium sulfide can react with sulfur to form sodium polysulfide, thereby playing a catalytic role.
对比例1Comparative Example 1
准确称取硫磺80g(2.5mol S)、无水亚硫酸钠315g(2.5mol)和水225mL(12.5mol)加入搅拌反应器,加热至125℃并控制搅拌速度300rpm反应10h,反应器中含有大量未反应的硫磺和无水亚硫酸钠,经检测,反应转化率低于80%。Accurately weigh 80 g sulfur (2.5 mol S), 315 g anhydrous sodium sulfite (2.5 mol) and 225 mL water (12.5 mol) and add them to a stirred reactor. Heat to 125° C. and control the stirring speed to 300 rpm to react for 10 hours. The reactor contains a large amount of unreacted sulfur and anhydrous sodium sulfite. After testing, the reaction conversion rate is less than 80%.
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