Document xd14DXVNEQ7M8j4vpj2pKJ5OJ

- . I'J * r* h7S*$i$$! , * ,vv ar __________ hr* ***** * a t Io y a i ; l i:..r * >-*> *-\i v -* *" * *- ? +~ I .41 ,, -.-I 111 liroadw?''. JNew ^orA. N. Y.. Acid Recovery. Bepc.' .mens PRQDpCIjS Vacuum Concentrators for. -' Spent Sulphuric Acid Chamber Acid- higher s;rength acid, it is .necessary; t.o ' booster which will create in .the concent, of up ,l 29.S". To avoid, .cpntem^ijign water v.-_- have also used`surface^,condensers'; the ba-.-uetric condenser. acuun .opling eaio1 P- Sludge Acid Vacuum Stills for Purification <of Impure Acid;; Vacuum Evaporators for ;-[ / Weak Solutions of Suphuric and Phosphoric Aci: Vacuum Coolers apd/CiysaIlx rs for. Acid Solutions-, -o COJMSTR1lie lJON A/' 'All cc-xentrators. are, of.splgta: 'i .Thefputside shell is;.ma4er-:bf. 01, /and .steel plate for larger.uruts.v. ,*1^0 sheets r chemical lead %e?.vto .^"';thick ;:JaU rexticaLe .;-and.-hor :ontal jointsp'are.burped ^jfn:j:H'o'Qptsi< ta'.mg - pectic. n and; /cpairs.*:i-,^g,-^eg.d'-`-13ning s - 1 5 r. Separating Plants for v ^ h Sludge Add pected a heavy,layer of aci^pro^ bricks laic y abl^ cement.j /Openmgs, are p.rotectgd- by"higl ^licgnj5- ;:-n:on?slecves^pThe.;ii^tdiig;surface'^onasl:s:;ofi<ar Blil pr o c ess Jead..or c.'ienu'c^lea^tubinglfw';stqam::pressure& In the .SimonsonJ^antras-^a< uum Process, patented .`>lbs.;5anc of:lead cojveredxoppcr:^bCs^OB;higi in the United States and -cforeig l countries, the .acid is iron.tuoes for a pressure uo|oil503b^A Conder sjhcpnTi- rgjg|n|i concentrated with.steam at from 5.1b. to 150 lb. pressure '. vacuum boosters aretmade o'f^har^ lead, special b under a vacuum of from 27" to 2 ^8" so that the boilin : or. iug.'. silicon iron. Where .necessary^ temperature of the finished acid sd . 'ftare:ef,,"oed with, eleo^rx11 F. The high vacuum practicallyjel AU i .aerators- crj r. u] r- The proper vapor speed, anil,low J losses due to entrainment and ch. one half of one percent No fumes concentrators. Well separated sludge acid is jus 60, 65, or 66 Be,j Spent`Aci^jai usually concentrated,to 932$.Utl brought-up to 95% apdp7$yJliigSt Invpll.^ases wherelthg^st^ngjl^ 9 . --* a " ' > .V *? & Conc entrator-ut 111are>IIkf iur Tyv1*r n1 '*J t r i up ii'r. vxi, tuui (<: v m- --8BT s..-: * w IHliul M IJin'I.l I M4 i' f *** s - - g&js ^ '.-V ij- v'**`rf . - - ... i t -i* a-v specially designed j .u i _ic. capacity auu operating condii tions for "which they-axe to be* used. We'fib not try b adapt one standard apparatus to' all possible Workm- conditions. '!* . , . ^, a p poomilN ''0 TStftfCESi. ;': ' Spent Acid. Large used in the chemical nitric acid and the ; Such dilute- acids are cur Super Vacuum efficiency. There ate inorganic impurities. 100-tons of H.gCV' Some of the sulphates which tor reuse. Sulpfo died in our special, difficulty and $re .v.itrifugals orva< Ferrous Sulphate ir under strict' Control Of otherwise the sulphate.' of a slime which efficiently. After and experimentation . pending, whereby under vacuum to an, ferrous sulphate1 is 56% acid, which no-jv phates, is further precipitated sulphate is,.,: irifuging in a coni sulphate residue is precipitate of the 36% acd ferrous sulphate can be jd^ ,... -...',1-,'vic acid in a chamber; O'f1 cOh a./oejcrecpvercci ny /conetsygg^ggg turn -mfsingle oridotfole'ieftecfetp about 30% acidity and1 the" fefrous fulphltd'^'r copperas br mcmohy^afe.^-fiAll, the1 acid ra the waste nquor is '' ** ' dich makes it i the. pickling ' I'., from a fusi- for lurther . acuum :pricenIosses hec^ssfirit,. these ;tp eliminate ACID STELLS . Sometimes the concentrated 'jspent acid cbntains inor ganic salts in solution, and whbre a technical pure acid is required `for -the process the| impure acid can be dis tilled imdertyacuum at* reasonable, cost. The distillate will ofrcc-ivrse be;absolutely freefronr these salts and the remaining sf ipfifiSil i 'SO that there is no lbfealbS^cid Ar `j; i UL>, ' j STALTJZERS of largb capacity tor lmpu: toe incrustations of the- cooling surface;. :We abd ^hepared to furnish com plete yacuuin ^CrystallizingjfiPiPnts-for the removal of Copper? >er and/fother- Salts :from waste acids. IP countries; several' of these' unite have been in continuous operation fdi'ii`M|i,fearSi ` ` 'Types A ^ao: i3D;!|fcoJae to . bu]ld a for. ^J|S;i stoouIjcJ,;!! Recbvfei Depai the exclusive rights and give licenses Process: Inquiries Lead Company, Acid New York. 000-NU-0000144S0