Method for preparing sodium polysulphides

专利摘要:
This invention relates to a chemical technology for producing alkali metal sulphides, in particular, to methods for producing sodium polysulfide. The purpose of the invention is to intensify and simplify the process. Into a stirred reactor lined with AlMgj alloy containing a melt of a polysulfide with a temperature of 300 ° C under an argon pressure of 50 Pa, alternating amounts of sulfur and sodium are introduced alternately in a liquid or solid state. Then for 2 hours, the stirring speed is reduced from 200 to 100 rpm while maintaining the reactor pressure 50 Pa. The resulting uniform sodium polysulfide melt is drained from the reactor into the molds and allowed to cool in a stream of argon until solidified. 2 hp f-ly. a f (l
公开号:SU1628852A3
申请号:SU853884938
申请日:1985-04-23
公开日:1991-02-15
发明作者:Биттнер Фридрих；Хинрихс Вальтер；Ховештадт Херберт；Ланге Лудвиг；Шплетт Эрих
申请人:Дегусса Аг (Фирма)；
IPC主号:

专利说明:

This invention relates to a chemical technology for producing alkali oxide sulfides, in particular, to methods for producing sodium polysulfide.
The purpose of the invention is to intensify and simplify the process.
The method is carried out as follows.
In a laboratory reactor lined with an AlMRj alloy, melt sodium polysulfide with a temperature of LLC ° C is loaded and kept under an argon pressure of 50 Pa for some time. Next, in a stream of argon, liquid sodium with temperature C is injected into the reactor in small portions through a charging nozzle with a glass pipette. After a certain amount of sodium has been introduced into the reactor, sulfur is introduced into the reactor through the funnel in an amount equivalent to the amount of polysulfide required.
During loading, the stirring speed is 200 rpm. In the next 2 hours, the stirring speed is reduced to 100 rpm. The pressure in the reactor while maintaining 50 PA. As a result of throttling or turning off the heat during the supply of sodium and sulfur to the reactor, the reaction temperature does not rise above 350 ° C. The finished reaction product is not fully filled by means of a siphon from the reactor to the baths and, in an argon atmosphere, is left for solidification. The method provides for loading sodium and sulfur into the reactor both in the form of a melt and in solid form, for example in the form
Mr. V

WITH
31628852
pressed wire. With STOM themes
The melt purature of polysulfides in the reactor is maintained / above the melting point of polysulfides in the range of 2UU - 600 ° C.
Example 1. Preparation of sodium tetrasulfide.
The process is carried out in a laboratory reactor lined with A1MR alloy resistant to the reaction medium. The reactor is equipped with a lid with connections for the loading of sodium and sulfur and a paddle stirrer and well pipe made of the same alloy. The volume of the reactor l-4 l.
2.970 kg of a melt is charged into the reactor with a temperature of l ZOO ° C as a residue from the previous operation. The reactor is kept under pressure of argon Pa. Before opening the charging nozzle, the argon flow is increased and the heated sodium liquid is injected in portions of l-3 g as in Example 2. Semi-sodium feed.
In the same way as in the example, containing 3,105 melts with argon temperature of 50 Pa, it is loaded with liquid liquid of 30 g and 62,609 j Q r mixing.
Quantities may be doubled
After mixing under conditions of reducing J5 ki from 200 to 100 rpm, 4.483 kg of sodium melts are drained, leaving 2.947 kg of melt for the process.
20 According to the analysis, the result is held: 32.20 wt.% Na (32.34%); 67.67 wt.% S (67.66%).
Example 3. Semi
using a glass pipette. After i-enter sodium sulfide. days l / 30 g of sodium, the equivalent amount of sulfur to form a polysulfide of 83.48 g is introduced into the reactor through a funnel. Then 30 g of sodium, etc., are again injected.
The amounts of sodium and sulfur injected alternately can be doubled and tripled. In general, the total amount of sodium is 1.176 kg, and sulfur is 3.281 kg.
During loading, the stirring speed is l / 200 rpm, in the next 2 hours the stirring speed is reduced to 100 rpm under conditions of maintaining the pressure in the reactor 50 Pa, 0
The temperature in the reactor is maintained equal to 350 C by throttling or turning off the heating during the loading of sodium and sulfur. After stirring for. A sample is taken for analysis from the obtained homogeneous melt, and then 4.565 kg of sodium polysulfide melt are drained from the reactor through flat drain pipe into flat baths with lids and in the atmosphere. The argon sphere is left for curing - s
| NIA.
According to the analysis, the target product contains: 26.25 wt.% Na (theoretically 26.39%); 73.67 wt.% S (theoretically 73.61%).
2.882 kg of sodium tetrasulfide is left in the reactor for the next process.
Into a reactor with a volume of 185 kg of melt at the same charge with that C, sodium sulfate is injected into 1.45 kg of melt at 4 11 0 ° C. The speed in this support
During the introduction of the polysulfide temperature is up to 230 ° C.
After cooling with a diluent of 10 ° C / 200 ° C for 240 s of 5 sulfur with a temperature of 14, the temperature of the melt does not change virtually.
Similarly, sodium and 101 kg of sulfur are introduced into the reactor, 45 this is 130 kg of pentasulfide Na4S j-.
Thanks to the thermostat, the temperature of the melt is kept for all sa l – 200 ° C.
At the end of the sulphide reaction, it is metered in, thereby being poured into a bath under cooling atmosphere, ground and the barrels are packed.
PRI me R 4. Paul Yes.
50
Example 2. Preparation of sodium trisulfide.
As in Example 1, a reactor containing 3.105 kg of residual melt with a temperature of 300 ° C under an argon pressure of 50 Pa alternately loads liquid sodium in an amount of 30 g and 62.609 g of sulfur when mixed.
Amounts of rechargeable sulfur and sodium can be doubled or tripled.
After stirring for 2 hours while reducing the stirring speed of the stirrer from 200 to 100 rpm, 4.483 kg of sodium polysulfide melt is drained from the reactor, leaving 2.947 kg of melt in the reactor for the new process.
0 According to the analysis, the resulting product contains: 32.20 wt.% Na (theoretically 32.34%); 67.67 wt.% S (theoretically 67.66%).
Example 3 Preparation of sodium pentasulfide
0
A volume of / v300 l containing 185 kg of a polysulfide melt from the previous load with temperature C is injected for 39 from 1.45 kg of sodium melt with a temperature of 4 11 0 ° C. The rotation speed of the stirrer is maintained at 170 rpm.
During the introduction of sodium into the polysulfide melt, its temperature rises to 230 ° C.
After cooling the melt with a coolant DL / 200 ° C, the reactor is sprayed out for 240 seconds with 5.05 kg of sulfur melt with a temperature of 140 ° C. At the same time, the temperature of the melt in the reactor is almost unchanged.
In a similar manner, 29 kg of sodium and 101 kg of sulfur are introduced alternately into the reactor over 8 hours, with 130 kg of sodium pentasulfide Na4S j- being produced at that.
Due to the thermostatting of the reactor, the melt temperature in it is maintained throughout the entire process at l-200 ° C.
At the end of the reaction, the polysulfide melt is quantified for another hour, then poured in an argon atmosphere to cool in a bath, and then crushed and packed tightly in barrels.
Example 4: Preparation of sodium disulfide.
0
Analogously to example 1, a reactor with a heat-insulated casing is filled with 1.162 kg of sodium disulfide melt heated by C.
Then, 3 gg of sodium alloy with a temperature of 120 ° C is injected into the reactor in portions.
After that, l-42 g of molten sulfur with a temperature of l-140 ° C is injected into the reactor.
The speed of mixing of the polysulfide melt in this case is l-200 rpm.
Similarly, 450 g of sodium and 627 g of sulfur are alternately charged to the reactor, after which the melt mixing speed can be reduced to 100 rpm for 2 h at an argon pressure n reactor / 50 Pa.
By throttling the pressure during the entry of sulfur and sodium melts into the reactor, the process temperature does not exceed 600 ° C.
The total amount of the desired product obtained is 1239 g.
Thus, the inventive method allows to obtain sodium polysulfides
For a different composition in several hours (instead of tens of hours by a known method), this simplifies the process of introducing reagents into an exothermic reaction.

权利要求:
Claims (3)
[1]
1. A method for producing sodium polysulfide, comprising reacting elemental sodium and sulfur in a melt by heating in an inert atmosphere, characterized in that
In order to intensify and simplify the process, the interaction is carried out in a sodium polysulfide melt with a temperature of 200 - 600 ° C with stirring in a reactor made of AlMgg alloy.
[2]
2. A method according to claim 1, characterized in that the sodium and sulfur are introduced in the form of a melt or in a solid
5 states.
[3]
3. Method according to paragraphs. 1 and 2, o tl i (assuming that argon is used as the inert atmosphere.
five

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法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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DE3436698A|DE3436698C1|1984-10-06|1984-10-06|Process for the production of sodium polysulfides from the elements sodium and sulfur|

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