SU71651A1 - Method for producing iron-molybdenum catalyst for decomposition of ammonia - Google Patents

Method for producing iron-molybdenum catalyst for decomposition of ammonia

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Publication number
SU71651A1
SU71651A1 SU9338A SU9338A SU71651A1 SU 71651 A1 SU71651 A1 SU 71651A1 SU 9338 A SU9338 A SU 9338A SU 9338 A SU9338 A SU 9338A SU 71651 A1 SU71651 A1 SU 71651A1
Authority
SU
USSR - Soviet Union
Prior art keywords
decomposition
ammonia
molybdenum catalyst
producing iron
catalyst
Prior art date
Application number
SU9338A
Other languages
Russian (ru)
Other versions
SU381212A1 (en
Inventor
Л.И. Вольфензоп
М.С. Промыслов
Original Assignee
Л.И. Вольфензоп
М.С. Промыслов
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
Publication of SU381212A1 publication Critical patent/SU381212A1/en
Application filed by Л.И. Вольфензоп, М.С. Промыслов filed Critical Л.И. Вольфензоп
Priority to SU9338A priority Critical patent/SU71651A1/en
Application granted granted Critical
Publication of SU71651A1 publication Critical patent/SU71651A1/en

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Description

Насто щим изобретение ripca.iaiaeTcr способ 1 риготов. катализатора дл  разложеиЕ  .The invention of ripca.iaiaeTcr is method 1 of rifot. catalyst for decomposition.

В качестве ноаител  алЯ rns-roTOB/ienHH катали:атора приолен ют промет 1и глину. Катализатором :лужпт железо, промстмронаиное молибденом .As a carrier, rns-roTOB / ienHH was rolled: the atoms were washed with clay and clay. Catalyst: ludpt iron, industrial molybdenum.

Изготовление катализатора о.-уи1ествл ют слалуюш гм сбразо:М.Catalyst fabrication o.wellable slalom um sbrazo: M.

На 100 г готовой смеси берут 42.8 г азот  окислог-о железа ;i 6.7 с молиб.лата -аммоии . Смесь co.ic;; раствор ют в 25 см лпстиллирова:-;иой воды. В раствор доб а-зл ют 10.7 г ,, выпариваю: воду и массу высушивают при 100°, после чего сдгесь ирока.и пзают до прекраЕНсдп  вы|Д|елени  окислов азота.Per 100 g of the finished mixture, 42.8 g of iron-and-iron nitrogen are taken; i 6.7 with molyblata-ammoia. A mixture of co.ic ;; dissolved in 25 cm of distilled: -; oi water. 10.7 g are added to the solution and evaporated: water and the mass is dried at 100 °, after which the mixture is removed and used until the oxidation of nitrogen oxides is stopped.

Полученную сухую массу топко изме.чьчают в порошок, просеиваюг через сито (560 на 1 см и к просе нной массе добгвгипст просе нпые через Td же оито шамот 2-1,8 г и глину 15 г. тптатсльно псремеиливают ,л добавл ют ,дистиллп уог а пн ую до пол чепи  тестообразной густой (массы, из которой -; изготовл ют шарпки.The resulting dry mass of the furnace is measured in powder, sifting through a sieve (560 by 1 cm and to the sifted dobvgipst mass sifted through Td with the same chamotte 2-1.8 g and clay 15 g. Before and before the floor, the dough is thick (the masses from which are; make sharps.

Полученные шарики сушат при 100-110° в течение 7-8 час., после чего их прокаливают нр:и 1000° IB .течсгие 7 час. Прок.;5леппые гп-арики состо т из глиНЫ, maiMOTa. окиеп же.чеза и окизи молпбдона.The obtained balls are dried at 100-110 ° for 7-8 hours, after which they are calcined nr: and 1000 ° IB. For 7 hours. Proc .; 5lepps gp-ariki consist of clay, maiMOTa. ochep zhe.cheza and oxide molpbdona.

Дл  aктивJaциlи каталл.-. тора окислы железа и молпбд ена восстанавливают до свобод ных металлов, что делаетс  непосрел.етвен,но ;В крсК-инг-аппарате дл  |разлож:ени  а1ммиака. В змеевик помещ-ают катализатора и при падогреве с постепенным подъемом температуры пропускают . Диссоциаци  аммиака вначале идет оче;-ь слабо, но с течением врелгвни происходит активаци  катализатора и ускорение процесса диссоциатдаи йММиака. Восстановление ведут в течение 5- 6 час. сначала при 500-600°-3 час., затем при бОО-750° в течение 2-3 час. О конце процесса восстановлени  по прекращению по влени  паров влаги в выход щей струе газа.For active Jati catal. -. Torahs, iron oxides and molpd-ene are reduced to free metals, which is done indiscriminately, but; In the cpc-ing-apparatus for decomposition: a1 miak. A catalyst is placed in the coil and, during cold weather, with a gradual rise in temperature, is passed. The dissociation of ammonia initially goes very slowly, but with the passage of time, the catalyst is activated and the dissociation process and acceleration process is accelerated. Restoration lead for 5-6 hours. first at 500-600 ° -3 hours, then at BOO-750 ° for 2-3 hours. About the end of the recovery process by stopping the occurrence of moisture vapor in the outgoing gas stream.

№ 71651No. 71651

Получанный таким способом катализатор через 6 4aic. после н ачала восстановл:ен1и  при 700-800° 97% разложени  аммиака. Через 3 мес ца практическопо испытани  катализатора никакого ухудшани  в качестве газа не устаиовлено.The catalyst thus obtained is through 6 4aic. after the start, it was reduced: en1i at 700-800 ° 97% decomposition of ammonia. After 3 months of practical testing of the catalyst, no deterioration in the quality of the gas was observed.

П 5 е д м е т и з о б р е т с ;н и  P 5 e d eme and z o breet s; n and

Способ получеаМШ железо-молибденового жаталиаатора ал  разложени  аммнака, отличающийс  тем, что раствор азотиокислого железа и молибдата ад1мони  смешивают с глиной, выиар|ИВаю т, высушивают и прокаливают, носле чего массу (измельчают, вновь омешн-вают с шамотОМ, глиной и водой в тесто, из последнего изготовл ют шарики иди зерна, которые сушат, прокаливают и восстанавд,ивают в 1Крек(И) гаппарате аммиа1ко;м при повышенной температуре.The method of producing an iron-molybdenum iron digester of ammonium decomposition, characterized in that a solution of iron nitrate and admonmonium molybdate is mixed with clay, extruded | Ivayut, dried and calcined, then the mass (crushed, again mixed with chamotte, glyme, | dough, balls of the latter are made from the latter, the grains are dried, calcined and restored, and they are fed in 1Krek (I) ammonia chamber; m at elevated temperature.

SU9338A 1943-12-27 1943-12-27 Method for producing iron-molybdenum catalyst for decomposition of ammonia SU71651A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU9338A SU71651A1 (en) 1943-12-27 1943-12-27 Method for producing iron-molybdenum catalyst for decomposition of ammonia

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU9338A SU71651A1 (en) 1943-12-27 1943-12-27 Method for producing iron-molybdenum catalyst for decomposition of ammonia

Publications (2)

Publication Number Publication Date
SU381212A1 SU381212A1 (en)
SU71651A1 true SU71651A1 (en) 1947-11-30

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