SU716585A1 - Iron catalyst regeneration method - Google Patents
Iron catalyst regeneration method Download PDFInfo
- Publication number
- SU716585A1 SU716585A1 SU782607856A SU2607856A SU716585A1 SU 716585 A1 SU716585 A1 SU 716585A1 SU 782607856 A SU782607856 A SU 782607856A SU 2607856 A SU2607856 A SU 2607856A SU 716585 A1 SU716585 A1 SU 716585A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- catalyst
- ussr
- catalyst regeneration
- regeneration method
- iron catalyst
- Prior art date
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
санй евлаги в газе не будет превьшатьsany evlagi in gas will not exceed
TsS TTrriSH feWBtfl grTfSS Ma ют до 48р-490°С. TsS TTrriSH feWBtfl grTfSS Ma up to 48p-490 ° C.
;; TaKofr вьсстановлёнй -fjjffgiji- -jjQji g - ff-gj;; TaKofr recovered -fjjffgiji- -jjQji g - ff-gj
тью 22,8 об..% аммиака при .Tyu 22.8 vol.% ammonia at.
При м а р . В установку, заполненную б Т окисленного катализатора/At m and r. In the installation, filled with b T oxidized catalyst /
HeiaSfeT Jfa3 с содержани еМ амми ак а 1,5% в количестве 45000 . HeiaSfeT Jfa3 with em em aka a 1.5% in the amount of 45,000.
р П ро-Цёсс восстановленй катализатора провод т при давлении 6-8 атм и температуре 450-49gi°C. Р езкйм восстайЪвленй приведен в табл. 1.A p-Zöss catalyst recovery is carried out at a pressure of 6-8 atm and a temperature of 450-49gi ° C. The recovery is given in Table. one.
...Т а б ли ц ... t a b
После восстановлени катализатор -гиесивируют и выгружают . Восстановленный катализатор содержит 80% металлического железа. Катализатор довос станавливайт в колонне синтеза в те , чение 1-1,5 суток. Активноеть катал,-, затора при , объемной скорости 30000 ч и давлении 300 атм равна 22,8 об.% аммиака. After reduction, the catalyst is hesiated and discharged. The reduced catalyst contains 80% metallic iron. The catalyst is installed in the synthesis column for 1-1.5 days. The active katal, -, congestion at a flow rate of 30,000 h and a pressure of 300 atm is equal to 22.8% by volume of ammonia.
В табл. 2 представлены сравнительные йагнйыёпб активности и содёржаник ) влаги в процессе восстановлени . Из э йТй данных видно, чтоIn tab. Figure 2 shows the comparative activity and moisture content of the recovery process. From this data it is clear that
при восс т н УвПёНии предлагаемым спо- собом ос йовна часть влаги выдел етс При сраёШтёльно нйзкйх температурах (450-470с) , когда отрицательноеwhen recreating with the proposed method, the axial part of the moisture is emitted at shallow temperature (450–470 ° C), when negative
вли ние влаги на активность катали- затора сказываетс в меньшей степени.The effect of moisture on the activity of the catalyst is less pronounced.
Применение данного способа позво- л ет по1вы С:йтьактИйнрсть катализатора и уменьЁгйтЁ расход энергозатрат за счет снижени температуры процесса, и давлени .The use of this method allows you to use C: catalyst inactivity and reduce energy consumption by reducing the process temperature and pressure.
Т а б л и ц а 2Table 2
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU782607856A SU716585A1 (en) | 1978-04-19 | 1978-04-19 | Iron catalyst regeneration method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU782607856A SU716585A1 (en) | 1978-04-19 | 1978-04-19 | Iron catalyst regeneration method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU716585A1 true SU716585A1 (en) | 1980-02-25 |
Family
ID=20761208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU782607856A SU716585A1 (en) | 1978-04-19 | 1978-04-19 | Iron catalyst regeneration method |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU716585A1 (en) |
-
1978
- 1978-04-19 SU SU782607856A patent/SU716585A1/en active
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