SU66494A1 - Sulfur dioxide enrichment method - Google Patents

Sulfur dioxide enrichment method

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Publication number
SU66494A1
SU66494A1 SU598-45A SU338921A SU66494A1 SU 66494 A1 SU66494 A1 SU 66494A1 SU 338921 A SU338921 A SU 338921A SU 66494 A1 SU66494 A1 SU 66494A1
Authority
SU
USSR - Soviet Union
Prior art keywords
sulfur dioxide
enrichment method
dioxide enrichment
gas
pulp
Prior art date
Application number
SU598-45A
Other languages
Russian (ru)
Inventor
З.П. Роэенкноп
Original Assignee
З.П. Роэенкноп
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 З.П. Роэенкноп filed Critical З.П. Роэенкноп
Priority to SU598-45A priority Critical patent/SU66494A1/en
Application granted granted Critical
Publication of SU66494A1 publication Critical patent/SU66494A1/en

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Description

11е(Ь(1ии, 1редст в.1Я1оииГ; с()6( i), a,U(()c:i.ii Kai 1;)трич и . об.иадает способностью R eo/uioii суспензии пог.моща .Пз cepiiiiстыЛ Ia,. При проп чк иии чс)ел TJIKVIO с. сисизик ccrnincTOio ItK-sM .110с .лелпн nor.ir.inaeicsj в : 1 ;1Мит( и.;11ч;ч-гипх iipii темпорат рнх.11th (L (1st, 1st c. 1H1); c () 6 (i), a, U (() c: i.ii Kai 1;) Trich and. Obv. And the ability of the R eo / uioii suspension to a great extent. Pz cepiiiiIstIl Ia ,. With the transmission of iHs) ate TJIKVIO S. Sisisic ccrnincTOio ItK-sM .110c. Helpn.n.

5;;л; и  с ciieirin;, иофс. Nii/ixci ior/iorii сернпстотч) г лз прмiHino и 2о раз оо, ЧСМ иола рапных ус/копи х.5 ;; l; and with ciieirin ;, iofs. Nii / ixci ior / iorii Cernstotch) g lz prmiHino and 2o oo, ChSM iola Rapa mustache / save x.

I ipc .:П1аг.И)1Й ciiocdo (jHoi-ai t сс|11:1 с;чим газа отличаетс  тем.I ipc.: P1ag.I) 1Y ciiocdo (jHoi-ai t cc 11: 1 s; the amount of gas differs in that.

ЧТ;: ,Ч:( KoliK) Неф;-, i;i ЧТСКМПК р а.тьа -;Л Я л iT в iipMieCce nor.lOHUH ,THU ;:, H :( KoliK) Nef; -, i; i CHTSKMPK p a.tya -; LI l iT in iipMieCce nor.lOHUH,

so. ло cooT:ioiiien;i l:/lv riDMNJepiio ::0 л.1  хстраиеии  образоваии:; :,-ГЛе;: ; 1,й.-1егчсЛ1и ; .кмуюи счо (рп/п.троваии .so. Lo cooT: ioiiien; i l: / lv riDMNJepiio :: 0 l.1 Education:; :, - GL ;:; 1, y.-1g; kkmoiu scho (pn / p.trovoi.

11 р и 1 с 1. ()тх()л 11и;е 1азь, )ло|1/л;11ипе SO- ь )1Соко1 ,1.с 7р;-Ч1;и, 1 аИ|;;1лгор -I ( к;)го:Л е iiosi-oMy кмгьиолчо 11сиол :-1онат1 1 роизвол.) ccpiioil . пропускают через 1у. содержаinyjo смесь .1ЬeaiiOiC) ;:(чЬолч1:а с кодоп ч/.п с оборотном раствором . Газ дропусхают через iieФe.лiиCJ: lJ . или путем барбота 1 а газопои струи через ny.it.uy, и,::; (M о-нииепи  .ii)noi: баиши с i pyGoii iaca;iKo.t, через которую газ.11 p and 1 s 1. () tx () l 11i; e 1az,) lo | 1 / l; 11ipi SO- ь) 1 Sok1, 1.s 7p; -H1; and, 1 aI, and | ;; 1lgor -I (k;) go: L e iiosi-oMy kmgyicho 11siol: -1onat1 1 bindling.) ccpiioil. pass through 1y. containing a mixture of .1BeaiiOiC);: (chich1: a with a kodop h / .p with a circulating solution. Gas is dropped through iieFe.liiCJ: lJ. or by bubbling 1 and gas jets through ny.it.uy, and, ::; (( M o-niiepi .ii) noi: baishi with i pyGoii iaca; iKo.t, through which the gas.

O6pa6( же.патедьпо 111-ои;1Л1Г -1 при Т(м11ерат |Н 3i и 1п:же. с не.НЛО Гю.тее к;.-|нон абсорбции .SO;.O6pa6 (same. Footed 111-oi; 1L1G -1 at T (m11erat | H 3i and 1n: the same. With no. ULO Gyu.tee to; .- | non-absorption .SO;;

В.1 ачале 1Л13ОМ ()6jia6aTi iBaiO гу., со.и |- жа1цу о око.ю двух веcOBi- ,x 4ficrcii жилкост ; ia o. весов чо чисть Т|-1(рдо1о материала, т. с. . lloc.ie того, как пуплта достаточно иасыти.тасв SO и иог.ющеиие ухудппьтось. :то пр01схолит арц сч).че 1/каиип SO; око.ю 120 ал. р збав.т5;от i:y.Tbiiy повым ко.чичеспигл к;.чк(сти. так ч .обы OTnouieinie Т:Ж ста.10 1 1--1:6. П|)и этом .чу.чьпа ст;-: -;о:лггс  виов) способно интенсивно 11оглои1ать SOs. После насыщении этой нульпы .ю содержани  SO 100 г/л иоггтощение оп ть резко уху.инаетс . тогда добав.т ют ио1зую порцию жидкости, так чтобы отношение Т:Ж составило около 1:10. Вновь насыщают пульпу SO; до содержани  80 г SOa в литре. При таком способе насыщени  с пос.чедовательным разбавлением не наб.1Юдаетс  образовани  студней, которое имеет место при насыщении пульпы с отношением Т:Ж больше 1:3.B.1 Achale 1L13OM () 6jia6aTi iBaiO Gu., Co.i | - to a woman about two eyes, x 4ficrcii zhilkost; ia o. weights cho tist T | -1 (pd1o material, t. With. lloc.ie how puplt enough iasyti.tasv SO and ioguyuscheiee deterioration.: that pr1 scholite art sch). 1 / kaip SO; oko.yu 120 al. from i: y.Tbiiy by new number of chicles to; .chk (sti. so t. OTnouieinie T: F grade.10 10 1 1--1: 6. P |) and this .ch.chpa v; -: -; o: lggs vov) is capable of intensely speaking SOs. After saturating this null .yu of SO content 100 g / l, the draining is again abruptly done. then add a portion of the liquid, so that the ratio T: W is about 1:10. Re-saturate the pulp SO; up to 80 g SOa per liter. With this method of saturation, with progressive dilution, a gel does not form. Jelly is formed, which occurs when the pulp is saturated with a T: W ratio greater than 1: 3.

Обработанна  указанным образом пу.чьна подогреваетс  до 50--60 н фильтруетс  дл  отделени  раствора от нерастворимого осадка.The material treated in this way is heated to 50--60 N and filtered to separate the solution from the insoluble precipitate.

Фильтрат нагревают до кипени ; при этом, уже начина  с температуры - 70° из раствора выдел етс  100%-ный сернистый газ, смешанный с вод ным паром.The filtrate is heated to boiling; at the same time, already starting with a temperature of - 70 °, 100% sulfur dioxide gas mixed with water is released from the solution.

Осадок, по.чученный после фильтрапии обработанной сернистым газом пульпы, может noirni на по.тучение OKHCJt алюмини , сульфатов ка;1и  н натри , и кремнекис.поты.The precipitate that has been sprinkled after the filtration of sulphurous pulp can noirni on OKHCJt aluminum, sulfate ka; 1N sodium, and silica crucibles.

П р е д м с т и 3 о б р е т е н и  PREDIMT AND 3 ABOUT THIS

(люсоб обогащени  сернистого газа путем обработки водной с)сиензни нефе.1ина разбав.ленным газом с последующей отгонкой концентрированного (обогащенного) газа из фильтрата, отличающийс  те.м, что суспензию нефе.лииа ностепен.чо разбав.-ипот в процессе поглощени  SOi до отношени  Т;/К примерно 1:10, с не.тью устранени  образовани  студней и об.-1егчени  процесса носледующего фильтровани .(condensation of sulfur dioxide by treatment of water c) nefen.1ina syngene with dilute gas followed by distillation of the concentrated (enriched) gas from the filtrate, differing in that the suspension of nephrodisaccharide dilute.-mortgages in the process of absorbing SOi to a ratio T; / K of about 1:10, with a lack of elimination of the formation of jellies and of an obscuring process of the next filtering.

SU598-45A 1945-04-24 1945-04-24 Sulfur dioxide enrichment method SU66494A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU598-45A SU66494A1 (en) 1945-04-24 1945-04-24 Sulfur dioxide enrichment method

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Application Number Priority Date Filing Date Title
SU598-45A SU66494A1 (en) 1945-04-24 1945-04-24 Sulfur dioxide enrichment method

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