Show r manufacture ot of sugar frim frio lb scientific dair jair un an i 4 j C liu Iru stIngs coil coll r t f do has his obtained abt lined a patent yr emmr i ci tle in N of 0 sugar sug sue arte arta spa ti 11 all arli which v ivl ivi v 0 e ruil full knowlt fc h ft nv importuna im ampon i ir a man maa tilt tiki titi tre ire this ell la it to a avira vers verv large CIAS oi our P r addi adb ads s th invention in apis ta ts in an fiode of treating cane tane jnice juice mola inola artt edic hent bent lie lle root juice other saccharine juines juices jda and syrup sma shA h hi ho purpose of 6 61 uin ulu m p g EU ir freed or sepa sepe riVed from fr im the yie imbur 8 and md oiher other sq tub tab feic C s with which it la is in mul mut axed it a b fa f t tj tine ne olAt fald tauf dald ld 9 sugar a 7 ad rm irom tine cine juice jnice sk in i beet row luce ance AW urt tit otar sac bardae juis jures juls la Is if i til lil t T r than thant it ought to be and ana the IV ca US f this small smail i d b ili lii as hn attributed to the tise TIM of biart al to cl r rity the h S rup whereby a 3 conifer cong frabie frable able abie pro of sugar bugar becomes absorbed orbed not withstanding mhd mus mos read rend that moia mola a by many ot of the X processes arn con coa nearly as much as 60 50 per cent of crysta crystalline U e engar augar for the th purpose of avoiding these evils the following process Is employ employed edThe edrhe thia thie aces molasses or syrups obtained by lir any at means from the sugar cane beetroot beet root or other plants conta malt matt matters lers are pan lian together with the quantity of ian ina 0 or lim lime ilme water ater ile gme eff ary aj P producing I 1 ng defecation jabout 30 39 or 40 per pet cent of lime Is sufficient for this purpose As soon as the limea has produced prod deed the requisite 1 fielt ripon tipon the liquid a quantity of I 1 I 1 of lime is wadded padded added to it for tor the tha purpose ol 01 neutralizing the lime usually in the of about 3 parts of the of lime ilme to loo parts of the te the s hog hoa P of nine may te at 4 beg feg fee I 1 beaumel Be aumea hydrometer hydro hydrometer neter or at any higher degree and ano it I 1 Is to be added as iong long lonea as any ary deddish litmus paper dipped upped into the Is turned blue should too much muth suller super i ahrne happen harpen tobe to be added 1 cary card can be by ali the immediate te addition addition of 01 as lime lim ort orl lime water as tbt th of lime in the solution will neui neut rallie 1 the mixture v trill ill by the tha at pro process gessy become r 4 and aid turgid arnd arid must bi belted 6 ered nip which I 1 I 1 iii ili may kiy bedo bado 0 dyl dyt 01 1 the oral ordinary n ary arv mann manner erth through it fa filtering kerine bags and the filtered juice joice or syrup Is pian to be i grated to i deau Beau deaume beaume lile ilie when then hen it mail malf gaj C Q me I 1 turgid or thickened for borha se of separating separ atins any impurities which 1 m may tty ity salier stu remlin remain in a in in i n the j dulco ulcia or syrup s 0 ot lime 11 Is again added so long iong lo ngIm tai lai litmus P paper pryl did dipped in irle juice Is turn turnell ed b blu biu U sater Saner a tha mixture passed through th filter and the filtered duld must so the tee f as much sugar as cat cal cai be ve s g A arateA erko in aeri leri manner and gud the vacuum panah pan and crystallizing tubs tuba may fel pel IL the usual way for this purpose Ee sugar retlaw lon lor pun pur nned ined in in this manner marner mar mai cien aier maba agaid dissolved or concerted conyer conter tel ted into syrup and again for tor the purpose of i further it f the crystallized cry sugar thus formed Is 11 ehen hen then to ber be separated I 1 usual way irom from the he resl resi n I 1 juice ot E rup with t 1 4 t w aich it Is afta 1 I 1 fro pro from m uli teis this s resit tuil juice 2 further quam ity off ugar sugar may mar bo be 0 taffies tam fied br bir th the tha 1 I wing process the jut jui cesor syrups 4 ard are haut laut diluted A N a oti UVA beaume with water or illif juice of beetroot beet root roo being pre ferredy and arid lim lime ilme or ume iter Is dededi idd wl I 1 and about ati 11 halt bait a as much ris ais s was s UJ lafor for tor the thearsa process will generally b t prodoc I 1 site defecation heat hiat 19 idehen then applied and before the syrup bolls boils adf deyrup syrup chases to any apparent alkil tae laa acton anthe ithe jt anday and by these means the phosphate of ax up be precipitated the cyru must pheaba filtered as belore becore bei bel ore ar for the pate purpose 01 pepa separating ratIng jj ls after filtered juice or syrup Is to ba be concentrate concentrate dand ind as before tor obtaining from it a I 1 further ur I 1 hrs quantity of sugary sugar C centrifugal biathlons Biath luns lons daay dway b be used for sep separation separ aratin atins the crystallized raie inie Jule jor sr the second residual saru bahls lat process may also als be subjected to the tha g fame an e princess aces J thit that lust just described for tor treating the first ars residual sittia byrn ta order I 1 I 1 to obtain fas pai aa r a further quality af pf 1 WS zad s suar ir to be separated from a 4 7 read es gypp sylph I 1 is as bafo before e in the same manner the process abife described may be applied to each cry nry xe remain atter after a previous process sg until the syrup oi of ace operated 0 upon apon shall be bar exha exhausted bed bygar or as niu diu mush h BO so I 1 I 1 as ma y to J economic economically aily dily f i since the english patent fees feea v mra pia rada reda at 40 the number 0 of f new inventions brought moio toto puMi has hag as beati constantly on the ine Inc reab collated arn brn newtons New tons london l paris i |