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SU108260A1 - Catalyst Regeneration Method - Google Patents

Catalyst Regeneration Method

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Publication number
SU108260A1
SU108260A1 SU559099A SU559099A SU108260A1 SU 108260 A1 SU108260 A1 SU 108260A1 SU 559099 A SU559099 A SU 559099A SU 559099 A SU559099 A SU 559099A SU 108260 A1 SU108260 A1 SU 108260A1
Authority
SU
USSR - Soviet Union
Prior art keywords
catalyst regeneration
regeneration method
regeneration
oxygen
catalyst
Prior art date
Application number
SU559099A
Other languages
Russian (ru)
Inventor
А.В. Агафонов
К.Е. Зегер
Original Assignee
А.В. Агафонов
К.Е. Зегер
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.В. Агафонов, К.Е. Зегер filed Critical А.В. Агафонов
Priority to SU559099A priority Critical patent/SU108260A1/en
Application granted granted Critical
Publication of SU108260A1 publication Critical patent/SU108260A1/en

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Description

Кол-во кок- Врем  полпа ка-та- ; ного выжилинаторе га 10 г кок1 г са 1 мин.Quantity kok-polpa ka-ta-; 10 grams per kilogram of ca. 1 min.

5(5,3 54,7 5- 1 48,6 42,9 37,55 (5.3 54.7 5- 1 48.6 42.9 37.5

Эти опыты показали возможность достижени  полного выжига кокса по предлагаемому способу за короткий промелчуток вре угени н получени  газа с высоким содержанием СО.These experiments showed the possibility of achieving complete burning of coke by the proposed method in a short run of time and producing gas with a high content of CO.

Пример 2. Результаты лабораторных опытов по регенерации синтетического алюмосиликатного дробленого катализатора на углекислотно-кислородном дутье (в кип щем слое).Example 2. The results of laboratory experiments on the regeneration of synthetic aluminosilicate crushed catalyst on a carbon dioxide – oxygen blast (in a fluidized bed).

Таблица 2table 2

Эги опыты показали возможность регулировани  температуры процесса составом дуть  и саморегулировани  температуры процесса горепи .These experiments have shown that it is possible to control the temperature of the process by the composition of the blowing and self-regulation of the temperature of the process of grief.

Практическую пользу предлагаемого способа регенерации катализатора , по сравнению с известным способом окислительной регенерации на воздушном дутье, трудно оценить без проведени  точных технико-экономических расчетов, возможных лишь при осуществлении проектной разработки всего комплекса процессов, св занных с организацией нового способа регенерации и рационального использовани  получающейс  окиси углерода в процессах синтеза.The practical benefits of the proposed method of catalyst regeneration, compared to the known method of oxidative regeneration in air blast, are difficult to estimate without carrying out accurate technical and economic calculations possible only when carrying out the design development of the whole complex of processes associated with the organization of the new method of regeneration and rational use of the resulting oxide carbon in synthesis processes.

Примерные расчеты материального и теплового балансов предлагаемого способа .регенерации с вариантом использовани  СО дл  процесса получени  водорода-дл  установки моп,ностью 3000 т перерабатываемого сырь  в суткиApproximate calculations of the material and heat balances of the proposed regeneration method with the option of using CO for the process of producing hydrogen — for installing a mop of 3000 tons of processed raw material per day

с выходом кокса-показывают, что в сутки можко получить 480 т СО. Превращение этого количества СО в водород за счет реакции CO-f-HjO- COa+Hj позвол ет получить т Hj в сутки и 750 да СО. котора  может вовлекатьс  в процесс регенерации катализатора. Стоимость получаемого при этом водорода примерно в ,7 раза ниже средней промыщленной стоимости его.with the release of coke, show that you can get 480 tons of CO per day. The conversion of this amount of CO into hydrogen due to the reaction CO-f-HjO-COa + Hj yields t Hj per day and 750 and CO. which may be involved in the catalyst regeneration process. The cost of hydrogen produced in this case is approximately 7 times lower than the average industrial value of it.

Предмет изобретени Subject invention

Способ регенерации катализаторов путем газификации коксовых отложений, отличающийс  тем, что, с целью получени  газов регенерации с высоким содержанием окиси углерода, используемой дл  синтеза химических продуктов , газификацию коксовых отложений осуществл ют углекислотно-воздущным или углекислотно-кислородным дутьем.A method of regenerating catalysts by gasifying coke deposits, characterized in that, in order to obtain regeneration gases with a high content of carbon monoxide used for the synthesis of chemical products, the gasification of coke deposits is carried out with carbon dioxide-oxygen or oxygen-oxygen blast.

SU559099A 1956-10-15 1956-10-15 Catalyst Regeneration Method SU108260A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU559099A SU108260A1 (en) 1956-10-15 1956-10-15 Catalyst Regeneration Method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU559099A SU108260A1 (en) 1956-10-15 1956-10-15 Catalyst Regeneration Method

Related Child Applications (1)

Application Number Title Priority Date Filing Date
SU813365158A Addition SU987357A2 (en) 1981-12-16 1981-12-16 Flat heat pipe

Publications (1)

Publication Number Publication Date
SU108260A1 true SU108260A1 (en) 1956-11-30

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
SU559099A SU108260A1 (en) 1956-10-15 1956-10-15 Catalyst Regeneration Method

Country Status (1)

Country Link
SU (1) SU108260A1 (en)

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