SU42545A1 - The method of obtaining sulfur from sulfur dioxide and hydrogen - Google Patents

The method of obtaining sulfur from sulfur dioxide and hydrogen

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Publication number
SU42545A1
SU42545A1 SU151336A SU151336A SU42545A1 SU 42545 A1 SU42545 A1 SU 42545A1 SU 151336 A SU151336 A SU 151336A SU 151336 A SU151336 A SU 151336A SU 42545 A1 SU42545 A1 SU 42545A1
Authority
SU
USSR - Soviet Union
Prior art keywords
sulfur
hydrogen
obtaining
sulfur dioxide
dioxide
Prior art date
Application number
SU151336A
Other languages
Russian (ru)
Inventor
А.Г. Рембашевский
Original Assignee
А.Г. Рембашевский
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by А.Г. Рембашевский filed Critical А.Г. Рембашевский
Priority to SU151336A priority Critical patent/SU42545A1/en
Application granted granted Critical
Publication of SU42545A1 publication Critical patent/SU42545A1/en

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Description

Насто щий способ имеет целью получение серы из промышленных газов, содержащих сероводород и сернистый ангидрид или один сероводород. Обычным  вл етс  прием получени  серы путем взаимодействи  сероводорода с сернистым ангидридом и, в частности, обычным также приемом  вл етс  окисление части сероводорода в сернистый ангидрид в тех газах, которые не содержат этих соединений серы в количествах , соответствующих соотношению: 2 молекулы сероводорода на 1 молекулу сернистого ангидрида.The present method is intended to produce sulfur from industrial gases containing hydrogen sulphide and sulfurous anhydride or hydrogen sulphide alone. Sulfur production by reacting hydrogen sulfide with sulfurous anhydride is common and, in particular, it is also common to oxidize part of hydrogen sulfide to sulfur dioxide in gases that do not contain these sulfur compounds in amounts corresponding to the following ratio: 2 molecules of hydrogen sulfide per 1 molecule sulfurous anhydride.

Известно применение катализационной среды дл  ведени  процессаThe use of a catalytic medium for the process is known.

ZHaS -f SOa - ZHaO + 3SZHaS -f SOa - ZHaO + 3S

и, в частности, применение в качестве такой среды раствора серной кислоты .and, in particular, the use of sulfuric acid solution as such medium.

Новый способ состоит в том, что серную кислоту берут концентрированную и процесс ведут при температурах серной кислоты 60-80°.A new method is that sulfuric acid is taken concentrated and the process is carried out at temperatures of sulfuric acid 60-80 °.

Новый способ в особенности пригоден дл  газов с повышенной концентрацией H2S, как например, дл  газов, отход щих при производстве ВаСЬ или BaSOi, технологический процесс произ (154)The new method is particularly suitable for gases with a high concentration of H2S, such as, for example, gases that are produced during the production of Bacillus or BaSOi, the production process (154)

водства которого протекает по следующим уравнени мwhich proceeds according to the following equations

BaSO4 + 2С 2СО2 + BaS BaS -f 2HCI BaCla + НгЗBaSO4 + 2С 2СО2 + BaS BaS -f 2HCI BaCla + НгЗ

или же из горючих газов, из которых сероводород выделен посредством химических реагентов, например, по методу „Sibord processor from combustible gases, from which hydrogen sulphide is isolated by chemical reagents, for example, by the method of “Sibord process

МааСОз + HoS : МаНСОз + MaSH,MAASOz + HOS: MANSOz + MaSH,

с последующей регенерацией воздухом или по методу „ПТИwith subsequent regeneration by air or by the method of "PTI

МазСОз + HaS : МаНСОз + NaSH с последующей регенерацией СОзMAPSO + HaS: MANSO3 + NaSH followed by regeneration of the POPs

SaHC05 + NaSH + C02 + 2МаНСОз + HaS.SaHC05 + NaSH + C02 + 2MANSOH + HaS.

Наконец, указанна  реакци  приобретает еще значение дл  р да процессов, где сразу получаетс  система H2S и SO-2, например , при восстановлении SOz вод ным или генераторным газом или активированным (древесным) углем (по методу проф. Юшкевича и Коржавина) или из колчедана при окислении его вод ным паром и т. д.Finally, this reaction becomes important for a number of processes where the H2S and SO-2 system is immediately obtained, for example, when SOz is reduced with water or generator gas or activated (wood) carbon (according to the method of Prof. Yushkevich and Korzhavin) or from pyrite oxidation with water vapor, etc.

Предмет изобретени .The subject matter of the invention.

Способ получени  серы из сернистого ангидрида и сероводорода путем взаинодзйстви  этих веществ в присутствииThe method of producing sulfur from sulfur dioxide and hydrogen sulfide by interfering with these substances in the presence of

серной кислоты, отличающийс  тем, что взаимодействие ведут в присутствии концентрированной серной кислоты и при температуре 60-SO sulfuric acid, characterized in that the reaction is carried out in the presence of concentrated sulfuric acid and at a temperature of 60-SO

SU151336A 1934-07-22 1934-07-22 The method of obtaining sulfur from sulfur dioxide and hydrogen SU42545A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU151336A SU42545A1 (en) 1934-07-22 1934-07-22 The method of obtaining sulfur from sulfur dioxide and hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU151336A SU42545A1 (en) 1934-07-22 1934-07-22 The method of obtaining sulfur from sulfur dioxide and hydrogen

Publications (1)

Publication Number Publication Date
SU42545A1 true SU42545A1 (en) 1935-04-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
SU151336A SU42545A1 (en) 1934-07-22 1934-07-22 The method of obtaining sulfur from sulfur dioxide and hydrogen

Country Status (1)

Country Link
SU (1) SU42545A1 (en)

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