SU395321A1 - The method of regeneration of hydrochloric acid - Google Patents
The method of regeneration of hydrochloric acidInfo
- Publication number
- SU395321A1 SU395321A1 SU1701128A SU1701128A SU395321A1 SU 395321 A1 SU395321 A1 SU 395321A1 SU 1701128 A SU1701128 A SU 1701128A SU 1701128 A SU1701128 A SU 1701128A SU 395321 A1 SU395321 A1 SU 395321A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- fluidized bed
- hydrochloric acid
- solution
- rate
- reactor
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/36—Regeneration of waste pickling liquors
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
1one
Изобретение относитс к способам регенерации сол ной кислоты из отработанного травильного раствора.The invention relates to methods for the regeneration of hydrochloric acid from spent pickling solution.
Известен способ регенерации сол ной кислоты из отработанного сол нокислогоA known method for the regeneration of hydrochloric acid from spent hydrochloric acid
травильного раствора путем высокотемпературного окислительного гидролиза. По этому способу окислительный гидролиз осуществл ют за счет нагрева раствора потоком гор чих газов до 8ОО-9ОО С в псевдоожиженном слое инертного материала, поддерживаемом этим потоком. В псевдоожиженный слой раствор подают после предварительного частичного испарени , а скорость потока гор чих газов поддерживают посто нной по всей высоте псевдоожиженного сло . Размер частиц инертного матери ала составл ет 0,2-2 мм.pickling solution by high-temperature oxidative hydrolysis. In this method, oxidative hydrolysis is carried out by heating the solution with a stream of hot gases to 8OO-9OO C in a fluidized bed of inert material supported by this stream. The solution is fed to the fluidized bed after partial partial evaporation, and the flow rate of hot gases is kept constant over the entire height of the fluidized bed. The particle size of the inert material is 0.2-2 mm.
Однако этот способ характеризуетс относительно низкой интенсивностью процесса. Так при регенерации отработанного травильного раствора, содержащего около 25% хлористого железа, удельна производительность оборудовани (по раствору) не превышает 15О л/м час рабочего объема реактора . Относительно высоки и удельные расходы энергии из-за высокой температуры , при которой осуществл ют процесс.However, this method is characterized by a relatively low intensity of the process. So, when regenerating the spent pickling solution containing about 25% ferric chloride, the specific equipment capacity (in solution) does not exceed 15O l / m hour of the reactor working volume. The specific energy consumption is relatively high due to the high temperature at which the process is carried out.
С целью интенсификации процесса предлагаетс скорость потока гор чих газов, поддерживающих псевдоожиженный слой, устанавливать в таких пределах, чтобы ее величина на входе в псевоожиженный слой превышала величину скорости на выходе из него в 3,5-6,5 раз.Нагрев 25%-ного раствора производ т при этом до температуры не более 450-60О С. Инертный материал представл ет собой гранулы со средним раз мером 3-15 мм.In order to intensify the process, the flow rate of hot gases supporting the fluidized bed is proposed to be set within such limits that its value at the entrance to the fluidized bed exceeds the rate at the exit of it 3.5-6.5 times. Heating up 25% the solution is produced up to a temperature of not more than 450-60 ° C. The inert material is granules with an average size of 3-15 mm.
При осуществлении процесса предлагаемым способом значительно возрастает его интенсивность, так как удельна производительность оборудовани увеличиваетс (до значени более 25О л/м.час рабочего объема реактора).During the implementation of the process by the proposed method, its intensity increases significantly, since the specific productivity of the equipment increases (to a value of more than 25 l / m.h of the working volume of the reactor).
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1701128A SU395321A1 (en) | 1971-09-24 | 1971-09-24 | The method of regeneration of hydrochloric acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1701128A SU395321A1 (en) | 1971-09-24 | 1971-09-24 | The method of regeneration of hydrochloric acid |
Publications (1)
Publication Number | Publication Date |
---|---|
SU395321A1 true SU395321A1 (en) | 1976-09-25 |
Family
ID=20489053
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1701128A SU395321A1 (en) | 1971-09-24 | 1971-09-24 | The method of regeneration of hydrochloric acid |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU395321A1 (en) |
-
1971
- 1971-09-24 SU SU1701128A patent/SU395321A1/en active
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