SU1357056A1 - Method of cleaning a gas from sulphuric anhydride - Google Patents
Method of cleaning a gas from sulphuric anhydride Download PDFInfo
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- SU1357056A1 SU1357056A1 SU853923568A SU3923568A SU1357056A1 SU 1357056 A1 SU1357056 A1 SU 1357056A1 SU 853923568 A SU853923568 A SU 853923568A SU 3923568 A SU3923568 A SU 3923568A SU 1357056 A1 SU1357056 A1 SU 1357056A1
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Abstract
Изобретение относитс к способу очистки выбросных газов от серосодержащих токсичных ингредиентов и;, может быть использовано в процессе очистки выбросных газов. Дл осуществлени способа очистки газа от сер- нистого ангидрида его восстанавливают монооксидом углерода до элементарной серы в двух сло х оксидного катализатора с использованием в первом по ходу газа слое железохромово- го катализатора при повышенной температуре . Дл снижени расхода катализатора и повьппени селективности процесса по сере слой катализатора располагают с зазором, равным 2-10 объемам первого сло , при объемном соотношении слоев, равном 1:2 по ходу газа, а процесс ведут при объемных скорост х газа в первом и втором сло х, равных 72-90 и 36-45 тыс-ч соответственно. При этом Чтроцесс ведут при 440-470 0, а также во втором слое используют оксидный желе- зохромовый катализатор. Селективность до 97,6%. 2 з.п. ф-лы, 1 табл. с ® сл САЭ СЛ О СЛ О)This invention relates to a method for cleaning exhaust gases from sulfur-containing toxic ingredients and ;, can be used in a process for cleaning exhaust gases. In order to carry out the method of purifying gas from sulfurous anhydride, it is reduced by carbon monoxide to elemental sulfur in two layers of an oxide catalyst using an iron-chromium catalyst in the first downstream gas at elevated temperature. In order to reduce catalyst consumption and reduce the selectivity of the process for sulfur, the catalyst layer is placed with a gap equal to 2-10 volumes of the first layer, with a volume ratio of layers equal to 1: 2 along the gas flow, and the process is carried out at volume velocities of gas in the first and second layers x, equal to 72-90 and 36-45 thousand-hour, respectively. In this case, the process is carried out at 440-470 0, and an iron-chromium oxide catalyst is used in the second layer. Selectivity up to 97.6%. 2 hp f-ly, 1 tab. C ® SL SAE SL O SL A O)
Description
1one
Изобретение относитс к способу очистки выбросных газов от серосодержащих токсичных ингредиентов и может быть использовано в процессе очистки выбросных газов от примеси сернистого ангидрида путем восстановлени ангидрида монооксидом углерода . The invention relates to a method for purifying exhaust gases from sulfur-containing toxic ingredients and can be used in the process of purifying exhaust gases from an admixture of sulfur dioxide by reducing carbon dioxide anhydride.
Цель изобретени . - снижение расхода катализатора и повышение селективности процесса по.сере.The purpose of the invention. - reducing catalyst consumption and increasing the selectivity of the process of sulfur.
Пример. На первую ступень реактора загружают 0,5 см катализатора со средним диаметром зерен 1,5 мм, а на вторую ступень - 1 см контакта этой же фракции. Свободный объем между ступен ми; 5 см, отношение объемов контакта первой и второй ступени 1:2, Суммарна объемна скорость потока газа 27000 ч . При температуре реакции и W 2,4 степень конверсии диоксида серы 96,8%, селективность по сере 97,3%Example. At the first stage of the reactor load 0.5 cm of catalyst with an average grain diameter of 1.5 mm, and at the second stage - 1 cm of contact of the same fraction. The free volume between the steps; 5 cm, the ratio of the volumes of contact of the first and second stages is 1: 2, the total volumetric gas flow rate is 27,000 hours. At the reaction temperature and W 2.4, the degree of conversion of sulfur dioxide is 96.8%, the selectivity for sulfur is 97.3%
Показатели каталитической активности при двухслойной загрузке катализатора (W 2,3+0, 1 ; , 5) приведены в таблице, где V и Vj - относительные объемы катализатора на 1 и II сло х; Vg - объем свободного пространства между сло ми, относ.; W - суммарна объемна скорость потока газа (тыс-. ; W - объемна скорость на первом слое (тыс. ч );, W - объемна скорость на второмIndicators of catalytic activity with a two-layer catalyst loading (W 2.3 + 0, 1;, 5) are given in the table, where V and Vj are the relative volumes of catalyst on 1 and II layers; Vg is the volume of free space between the layers, relative .; W is the total volumetric gas flow rate (thous;; W is the volumetric velocity on the first layer (thousand h) ;, W is the volumetric velocity on the second
1one
1357056213570562
слое (тыс. ); ofco степень ис-- пользовани монооксида углерода (%);layer (thousand); ofco degree of use of carbon monoxide (%);
So,So,
- степень конверсии диоксида се-- degree of conversion of dioxide -
5five
ры (%); Z gj - селективность по сере (%); t - температура (С). оry (%); Z gj - sulfur selectivity (%); t is the temperature (C). about
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU853923568A SU1357056A1 (en) | 1985-05-13 | 1985-05-13 | Method of cleaning a gas from sulphuric anhydride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU853923568A SU1357056A1 (en) | 1985-05-13 | 1985-05-13 | Method of cleaning a gas from sulphuric anhydride |
Publications (1)
Publication Number | Publication Date |
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SU1357056A1 true SU1357056A1 (en) | 1987-12-07 |
Family
ID=21187183
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU853923568A SU1357056A1 (en) | 1985-05-13 | 1985-05-13 | Method of cleaning a gas from sulphuric anhydride |
Country Status (1)
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SU (1) | SU1357056A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994019102A1 (en) * | 1993-02-26 | 1994-09-01 | The Regents Of The University Of California | Catalyst and method for the reduction of sulfur dioxide to elemental sulfur |
-
1985
- 1985-05-13 SU SU853923568A patent/SU1357056A1/en active
Non-Patent Citations (1)
Title |
---|
Патент СССР № 3888970, кл. В 01 D 53/34. 1975. * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994019102A1 (en) * | 1993-02-26 | 1994-09-01 | The Regents Of The University Of California | Catalyst and method for the reduction of sulfur dioxide to elemental sulfur |
US5494879A (en) * | 1993-02-26 | 1996-02-27 | Regents, University Of California | Catalyst for the reduction of sulfur dioxide to elemental sulfur |
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