@i,913,749 a i@mperat7ure of @bout 300; C as OthetWise some of the crystallit(@d Steb@ins acid may go back- into solution and isomerize, thereby decreasing the yield. In diliitilig I the completicn of the sulfonation mixture ' at 1 the sulfonation, the sulfonation inixture ma3, -also be added to water efficiently cooled and agitated so that the tempbratu@e 6f the diItited inass does not exceed abolit 250 C. Inio stead of Filter Cel other equivalent filteii aids may be emplo-ved io assist in the reinoval by hltratioii of ., the small aiiiount of finely di'Vided inaterial present in stisoeiision in the clilution mixture. The Stebb-ns acid may 15 be salti@d out of the dilution mixture by other suitable alkali-Metal salts, c. g., 1)6tassilliyl chloride, etc., and the Stebbins acid alkalimetal salt may be filtered at 6ther temperatures. A filt@ation teinperature not exceed2@O in- about 2@50 C. is preferred, 1-iowever, )n oraer to prevent undtie 16ss of product by soluti6n in the inother liquors. The inventi6n thus affords a means of seetiring an increase iii the yield and in the 5 bbins acid,-D 4uced from betapuritv of Ste ro naphthol by sulfonation with stilfuric acid Since certain changes inay be inade in the process above@ described without departing from the sco@e of the invention, it is intend30 ed that all -nlatter contained in the above deser.ption sliall be intei-preted as illustrative an@4'not in a limiting sense. It'is al-,o to be uiiderstood theit @the following claims are inteiided to r 6o@er ,ill of the gen@6ric aiid specific features o@f the invention herein described. I cillim l@ Tn the I)rocess of pr(@paring,, Stebbins acid bv the sulf onat,ion of beta-na@lith6l with 40 Nem.@nt concentrated stilf ui@ic acicl, the impr6 which co prises rei,n I oving froin the spliere of the reaciion, a@ soon aq possidie, the Stobbins acid formed. e p@oces@ of preparing Stebb' 2 In th ins ,teid by the sii1fonation of- I)eta-na phthol with concenti-ated sulftii@ic acid, the imi-)rovem6nt -w@ich coniprises iiiducino,, crystaliiza-tion of Stebbins a,cid f roill the i@eacti;n ii.-iixture suibstan.tially as soon as ti-le react@ion mixtiire beCoTnes supersatur,@ted tl-iet@with. 3. 11-i the 13rocess of prephting Stebbins acid by't-he s Lilf onation of betaiiaphthol with concentr,,ited s@lf uric acid, the iinprovement @vhicb. coin@riseq seie'din- t,he @ea(-.tion mix65 ; I stibsta@tia-113, as soo@ as it, Decoine-s sa,ttir@ied'with Stebbiiis acict 'to cause the Steb,bins aci@l f orme @d to cryst,,illi ze. 4. Iii the i3ro@ess of pi@epariiio- St,ebbins 11 9: 60 icid by the, stilfpn,,Ition of-@beti-naphtbol ivith concentrated stilfi-iric acid. the iiaprovel-nent which conlprises adding a crystal of Stebbiiis acid to the repetion mixture ds a seeed @ubstaiatially as sobn as tile reaction inixtilre be65 comes saturated witb Siebbins acid@ ivherebv th" Stebbins acid f ori-ned is caused, to crystallize. 5. Iii the process, of preparin . Stebbins I 9 acid by the' siilfon,,'ttion of beta-naphthol with coricelitrat d @i-ilftiric acid, th ' e iiiiprovement '70 N),Iiich eoiiiprises aclaing a c.rystal of an alkali-iii(@,tal salt of Stebbins a6id to the reactioii iiiixttire as a seed substantially as @oon aq the re,,ictioi-i@ illixttire becoiiies sattirated inrith Stebbiiis acicl, wli.ereby the Stebbi-ns acid 75 'foi-iiied is caused to crysta-Ilize. @6. In the process of preparing@ Stebbins t qlcid by he stilfonatioii of bet-a-iiaphthol with c oncentr,,ttecl. stilfuric acid, the iniprovement Nvhich comprises adding the beta-naphthol so to the sul.f.Liric a(@id wit,hii-i a peri6d not exeeediiig 5 li'liniites, aiad causiiig the Stebbins acid to crystallize f roin the reaction illixture slibstanti Ily as sooia as the reaction mixture becomes sti.persattirated therewith. 85 7. In the @pi-ocess of preparino,@ Stebbins ilcid by tlic, sLil.f6nitioii of betanal)lithol with colicentr,,tted sulfiii-ic acid the iinprovement ich coniprisee@ '"7h , rtpidly'addiiig tl-te beta i-ilphthol t tl-ie stil@ur'j acid pre-cooled to 9(, 0 1 It t@ilipertture, n6t elxceedino, 5o'C. and com@ 1.)leting the siilfonation @at a temperattire not e-Neeeding abolit 25 lo C. 8. In the pr6cess of prepai-ing St-ebbins acid b3, the stilf onation of beta-in a,phthol with fl@j@ conceiitt,cited sLilftii-ic acid, tl-ie@ ii-nprovem'ent %vliieh conipiises rapidly addino, tlie'beta@n n,,iphthol to ti.le stilftiric acid pre-cooled to Itiot exceediiig abotit 5' C., C a, te,'-"Perature I OMpleting tho sulfonttion at a ten-iperafure of I( abotit @Oo to 25o C., @iid adding the completed s-Lilfoi-i,,tt-ion niixttire witlio@t delay to ice wat6i-. 9@ The pro-,ess of prepa-vino,, Stebbins acid %,hich coiiipriz@es acldiiig ivithiii a. p6riod not exceedinz 3 minutes about 100 @parts by 'vveight of beta,-naplitliol t6 abwit @00-2@b pai@ts b@- weigb.t of 98 to 100 @er (@ent. sulfur@ic a Lir cid ivhile @reveiiitin,g the teii-ipera-t P, f'rom exceeding aboui. 2,5' C., and C.,tusinv the Steb il' bn,@ acict to crystallize from the redetion n-iixI re ubstaiitially as soon as tl-ie nixtu s tui-e becoi-nes supersaturatecl tlierewith. to. The process of preparing Stebbins'acid 117hicli coml)rises t,ddiiio, withiii a period not liL@ xceeding abotit 5 iiiintites about 1.00 parts by e weight of beta,-naphthol to about 20OL280 )arts by weigl-it of about 100 per cent, sulftiric cid, while 1)1.eveiitill,- tl-ie t@mperatlire from exce@dinz iboiit 2,@@' C., and adding a crystal of Stebbins acid to the react@ioii n-iixt.ui-e as a S66d about 8 to 13 ininutes after the betanaphthol hts 'all been added, whereby the Stebbins acid f oriiied is caused to crystalliz4e@@ 11. The process of prep,,triilg Stebbins acid which comprises adding within a period not exceeding about 5 minutes aboiit 100 -Darts by weiglit 6f betanaphthol to about 200-230 yoarts b.17 weight bf about 100 per ceiit. stiliuric@a@id@cooledtoatemperatureofabollt5, 4 1,913,748 C., adding- a crystttl of Stebbins acid to the reaction mixture as a seed about 8 to 13 i-ninut6s after the be'tanaphthol has all beeii added, whereby tlie. Stebbins acid forn-ied is -,aused to crystallize,, ancl continuidg the sulfonation until substantially all of the betanaphthol has been sulf onated. .1 12. The process of preparing Stebbins acid which -0'1-' 'rises addin- within a pei-iod no'u ' 10 i ceeding al-out 5 minu-tes abotit 100 p,,trt by -.X s weight of beta-iiaphthol to abotit 200-230 pdrts by -%veight of 98 to 100 per ceiit. sulftiric acid while preventin@2@ thetemperature from exceeding about 25' C. and causing the Steb@ins acid to crystallize froiii.the reaction inixttire substantially as soon as the reacti6ii tnixtiire becomes stipersatlirated tlierewitli. 13. The process of preparin,- Stebbins @icid which comprises adding within a period not 20 about 5 miliiites aboiit 100 parts bl, 'Weiglit @f beta-naphthol to about 9,00-9,9) parts by weight of about 100 per cent. sulf itric acid cooled to v@ temperatlire of about 50 C.@ addino, a er I stal of StebbiTis acid to ttie y 25 -eacti u on mixture as a seed abo t 8 to 13 ininutes after the betanaphthol has all beeii added, whereby the Stebbins acid fcrmed is causecl to crystpllize, continuiiig the sulf on,-,tioh until substantially all of the beta30 @iaphthol has been sulfonated, wliilc-, preventing the tenipera'ui-iro fr6in oxcoedin@2@ about 300 C dilutin(y the resulting sLill'o-natioTi ii,ii,kti,ire with cold water without del-- Y, aiid sepai-,,ttiiig the @Stebbins acid. 35 14. The process of preparin Stebbiiis acid 9 which coliiprises adding within a periocl iiot exceding about 3 minutes about 100 parts by Wei,-lit of beta-naphtl-iol to about 200-230 .1 @irts b oiit 100 per cen . p y ivbight'of ab t siil40 furie, acid cooled to a tein erature of ,ibout PI 50@ C., adding a crystal of St6bbins acid to the r,-acl@-ion mixture as a seed about 8 to 13 ii-iinutes after the beta-iiaphthol b.as all beeii added, wliereby the Stebbiiis acid forin(@d is 45 -aused to erystallize, cont;.D.uing the stilf ojii ti6n at a temperature not exceeding 30' C. for about 30 mintites after all of the betanaplitliol has beeii qdded, and dilutin(,, the ilesi.ilting sulf on-,ttion mixt,,ire without delay 50 -@,vhile prei,entin- the temperattire from ri-@i--ng above 25' C. 15. The process of preparing StebbiTis tcici Whi6h coin I prises adding -within a period, iiot exceeding @ibout 3 inintitesibout 100 parts by r)5 -,veight of beta-naphthol to about 200-230 parts by w6ight of about 100 per cent. stilfuric acid cooled to a teml,)erature of about 5' C.) addin(y a crystal of Stebbins' acid to the reaction n-iixttire ,@s i seed about 8 to 13 iiiinutes co after th6 beta-naphthol has all beel-i added, whereby the Stebbins ,tei-d formed is cail@-@ed to crystallize ' cont;-n,,iin,- , the siilfonation a'Ll a temperature not exceeding 25 0 C. for about 30 minutes after all of the beta-iiaphthol h,,,ts 05 been added, diluting the resulting sulfonanion iiiixture without delay while preventing tl-ie teinperature from rising above 250 C., and salting out the Stebbins acid. 16. The process of preparing Stebbins acid which comprises addiiig within t period liot exceediiig about 3 minutes about 100 pai-ts by weight of beta-naphthol to about 215-220 parts by weiglit of 100 per cent. sulfuric ' acid cooled to ateiiiperature of about 5" C., adding a crystal of Stebbins ae'd to the reaction 75 I mixture as a seed abotit 8 to 13 minutes a'l.ter the beta-naphthol has all been added, whereby the Stebbins acid f ormed is caused to ervst,@tllize, continiiing th-, sulfonation at a teiuperattire not exceeding 30' C., for about 30 80 ininutes af ter all of the beta-na _phthol has b,-eii added, while preventing the teiiipera7 ture froiii exceedino, about 301 C., diluting the resulting sulf ontlion mixture without clelay while preveiitiii tl-ie teinpei-ature -L'rom 85 9 ris,.ng abov(- about '@50 C.@ filteriiig off insoluble in,,iterial, salting out tl@e Stebbins acid by n-ieans of sodium chloride, and separating tl-ie Stebbins acid sodium salt. 17. Iii ' e process of preparing Stebbili uh $90 acid by siilfonating beta-naphthol with concentrated sulfuric acid, the improvement which coinprises reinovin@y the Stebbins acid foilmed fi-om the sphere of reaction by causing it to crystallize out of the solution whilo 05 continuin- the stilfoiiation of the beta-na h2@ p thol. 18. In the process of preparing Stebbins acid, by sulfonatina beta-naphthol with concentrated sulfuric acid the improvement '10( which comprises adding crystallized Stebbins acid t6 the reaction mixttire substantially as soon as it becoines saturated therewith, s whereby the Stebbin acid forrned is caused to crystallize, and Continuin,- the sulfona,- 105 tioii of the beta-naphthol, the Stebbins acid continuing to crystarize out as formed. 19. The process of preparing Stebbins acid which comprises rapidly adding about 100 parts by weight of beta-n,,tphthol to about l@10 200-230 parts by ivei-'@it of 98 to 100@'o sulfuric acid while prev@ntiiig the temperature from exceeding about 250 C., and causing the Stebbins acid to crystallize fron-i tl-ie reaction mixture about 8 to about 13 minutes 115 after the beta,-naphthol has all been added. 20. The process of preparing Stebbins acid which comprises adding witliin a period not exceedin- about 3 ininutes, about 100 parts by weigi@t of beta-naphthol to about 200-230 120 parts by weight Of 98 to 100@'o sulfuric acid precooled to a temperature not exceeding about 50 C., and causing the Stebbins acid to crystallize from the reaction inixture about 8 to about 13 minutes after the beta-naphthol 125 has all been added, while@ maintaining a temperature not exceeding about 30' C. 21. In the process of prepariiig Stebbins acid by sulfonating beta-naphthol with concentrated sulfuric acid, the iniprovement 130 i,913@748 which cqmprises reirioving the Stebbins acid f,ormed from the sphere, of the action by causing it to crystallize out of s6lution substantiallv as@soon as the reaction mixture becomes supe I rsaturated therewith, and coii' tinuing the siilfonation Of the betanaphthol at a temperature not exceeding about 300 C., the St@bbins acid contiiiuino-, to crystallize oiit as formed. 10 22. I:n the process of preparing Stebbins acid by sulfonating beta-naphtliol with concentrated stilfuric @cid, the improvement wliieh comprises rapidly addin- the betanaphthol to 93 to 100@'o sulfuric acid pre@j cooled to a temperature not exceecling about 15- C., causing the Stebbins acid to crystallize from the reaction mixture about 8 to about 13 min-Lites after the, betanaphthol has ,tll been added. and continuino- the sulfonaI the Ste i s acid (.0 tOn of the beta-nap n I continuing to cryst out as f ormed. 23. In the prcicess Of prepariiig Stebbins acid by E;ulfonating beta-naphth6l with cOncentrated sulfuric acid, the improvement which comprises rapidly adding the betanaphtliol to 98 to 1:00@'o siilfuric@ acid precooled to a tempei,ature n6t exceeding about 5 o C.' causing the Stebbins acid to crystallize from the reaction mixture about 8 to t) @ibout 13 minutes after the beta-naphthol bas all been added, and continuinz the sulf6nation of the beta-naplithol at a teiiiperature ii6t exc@ceaing about 300 C., the Stebbins acid continuing to crystallize out as formed. In witness whereof, I have hereunto set MY hand. WILLIAM J. COTTON. 40 45 50 55 60
Patented june 139 1933 1 9139748 T@TN '-D STATES PATENT 1 E ; OFFICE @@ILLiik J-. COTT019-,'07''@BUFFATO, NEW YORK. ASSIGNOR TO;NATIONAL .4L]@ILINE,'& c micir, compaiy. ixc.@ OF NEW YORK,@ N@ Y@, A CO:@.PO'RATTON F I%TEW YORK 0 PROCESS Olp PREPARING STEB33INS &CII) NO Drawing... Application flied November 15, 1929. Serial No. 407.578, This inveiltion relates to the preparation Plf Stebbins acid (2-1- iaaphtholsulfonic acid), and it, r@l@tes. p@rticula@iy to i Daprovements iii the pr-ocess of prepariiig Stebbins acid by the sulfonaiign @f beta_naphthol (2-naphThe pi@incipal ob @ect of the invention is to ii.icrease tlie,yield o,f Stebbins @cid obtained ill ih@ si@lfonation of @beta-nadhthol with con@A9 centrated sulf,uric acid. Anc@ther obj@et of the in@entioll is to inC-rease th@. urity@ 6f the Steb-hins acid obtained in @ tK@ sulfonation@ of beta-naphtliol with sulfuric acid. Othei obje@ts of i@he invention will in part b@@ obvious aiid will @ii@ part appear here'lnafter' Will@ii @beta-@@phthol is sulfonat@ed with sulfuric acid accordinrg, to known pilocesses f cr 90 -e'@ro et on of Steb'L@ins acid, there is Droth .4@c@d a mixture c6mprising $tebbins @cid (2.1-na@htliol-s@ilfonic acid) and Bayer's acid aphtholsullortic @cid) togeiher with soin@ S@liae:ffer's 6(,id '(2.6- naphtholsulfonic op(rtioiis. 1 h@ve, found acid@ in - @ar@ino, pr in the sulf onat@i@n of beta-naphthol with stil@u@ic @ acid for the proauction . ol' Stebbins acia, th'at if the Stebbins acid prodii@ed is reiijo@i,@d'from the si)here of,the reaction prac@,@,@,0 ti@ally as soon as possible, the yield o,f Stebb@n@ @cid is increased wh@ile the amount of @@4y@-er s acid@Droduced is correspondingly de.crease:d :'@ The @resent, invent.ion acecr@ingly 'ComDrises @he application of the"ab6ve discovery t6 the preparation of Stebbins acid by the sulfonati6ri of beta-naphthol. The invention @w'ill @be exe @lified. in the process hereinqfter. disclosed; and its@ scope will be 40 iiidicated in'the claims. @'In the @ractice of the present invention the pbjeci@ t@ereor are, accom.plished by teacting b6ta,ii[itphthol With co-neentrated sulfuric ,i@ld ii[nder such @oriditions that the Stebbins ii,@ld as @orihed is catiseci to separate from the solution sab@tantiall@ @s @s6on as the reaction @@m@ i@@r6 be@omes su )ers@turatod therewith, 6r I so6ii t hereafter as is possible, and the @suloii is conti @d @uiiiil it is coin@lete. f t' nil The Stebbins aci.d n-iay be tlieii separated i'roiii the reaction mixture. Iii carryino out tlle process of the invention in a ccoi@danc@witli a preferred inethod of procedlire, beta-naphthol is added, preferably in 55 @i miniinuiti aiTi6unt of tini'e, to concenti-@tecl siilfuric acid at a temperature not exceeding about.250 C. When the reaction mixture becoii-ios supers,,tt-Li atecl with respect to Stebbins acid, the Stebbins acid is caused to crys- @og tallize out of solution, thereby rem it ovin i'@oi-ii the spliere of the reactio@, and the Su T-onation is allowed to, continue until substantially all Of the beta-naphi@hol h.as been iulfonat@d, the Stebbins acid continiiing to @65 ci-ystallize otit as it is formecl. The Stebbilns acid iiiay tl-ien he separated froiii.tl-ie sulfoiiat;ioii n@ixtuie; as fol- example, by dro.ivniiig in water while preveiitil-ig the temperat.Lire from risino, above the poi@it where iiiidesi.red :.7,0 tn liycli,olysis of Stebbilis acid occu@s, filterln"g to' reii@ove traces of insolubles present, Salting out acid witli a suit l@ alab li-in e alkaii1;:a e filteril @g off metal sa t s i @cid thereb The beta-na ol eiiiplo3,ed is ()f'a. high o-i-a f piirity and iii vided forin'. ease of operatio ed N-,, i thagita to, a bitt6h of sul@furi cid preco6led to a teiiipei-,attire iaot exceeding 59 abotit 15" C., pref(,,rabl@@ iiot exceedinz about 5' C. The sulfuric acid @ i-iiay vary in concentration fr6iii about 93 per cent. to,100 per cent., H,SO,, acid of 98 Pell ceiit. to 100 per eiit. concenti-atioi@i being preferred. 'the @85 t)eta-i-iaplitl-iol is added as i-apidly as.possible, a iii@xii-nurn period of titile@ for the addition beiii(r al:oout 5 to 10 iniiiutes depeTidiln'@, @n the stre,nath of ,teid ),nd te]]Llpe@,ittire = and a i)eriod of tiitie iio@6 ex@ ceec" ol Lin(y 3 @n iiainu beiiig pi,eferred. In orcler to pre I -i, -i o vent ftr as is possible, the forii ttioi f Baye acid (2@8-iiaphtliolsulfonic -Leid) tl-i@ll Steb acid fori-necl is rel-nove(i fi@oin the sphere of the reaction as sooii a possible. Tliiq may be brou(yht tbout by C"tLls;-Ilcr ti'le Stebbins aeict to c@rystallize ou't of tjae "'react' 1.011 I on as the reac@t@ioii i-rixttire b rated tllere-witli. It some, it the Stobbii@,3 acid W'll 2 1,913,748 sr.iontaneously crystallize from the reaction mixture; but, unless the crystallization is caused to take place witl-iin a niiniiiaum period of time, after the reaction mixture has r) become saturated therewith, the yield of Stebbins acid will be decreased and the production of Bayer's acid will be increased. If crystalization of the Stebbins acid fails to occur when the i-ea-etion mixture becomes 10 saturated or @upersaturated w-Lth respect to Stebbins acid, crystallization is incluced by seeding the reaction mixture with a small portioii of crystals ol' Stebbins acid. For convenience, the seecl is preferably a por15 tion of a previous sulf ongt-i on mixtiire saved foi- the purpose. Wheii operating witli 98 per cent. fo 100 per cent. sulfuric acid, the sulfonatioii mixture is preferably seeded withiii about 8 to about 13 minutes a r 26 all of the,beta-naphtliol has been adcled; with weaker acid, which requires a longer time for the sulfonation, seeding is not e:ffective to produce crystallizati6n until a somewhat later time. The sulfonatioii is referably allo*ed 2r) to continue until a maxiiiaum amount of Stebbins acid is obta,.necl,- the Stebbilis acid continuing to er37sta'il-ize otit as it is produced. The reaction may then be interrupted, in order to prevent loss of the Stebbins acid 30 pi,oduced, by diluting the react,,o-n mixture, while preventing the temperature of the dilution mass from rising ex(, -essively. This may be brought about by aclding the sulfonation mixture witli ao-itat-lon, at the comple3r) tion of the sulfonation, to ice, or to suita.bly cooled water. The Stebbins acid, which goes into solut-lon in the dilution liquid, may then be separated from the solution, preferably following a filtration of the dilutioii liquid '40 to remove any u i-ilf onated bet ns a-naphtliol or othe,r insoluble h-iaterial preseiit. This may be effected in a nuinber of ways; e. 9-@ by neutralizin- the solutio-n with lime, limestidne, calcilim sulfite, etc. , filterina off the 45 calcium sulfate formed, converting the, calcium salts to sodium or 1)otassiuiii salts with sodium or potassiuiii ep.@bonate, sulfite, etc., filtering olT the ea-leitim carbonate, or other insoluble calcium salt, and sillting out the 50 sodium or potassium s,,tlt of. Stebbins acid; by extractinz the Stebbins acid w-th a suitat@le solven@- by neutral;.7,ing the solution with caustic alkali, and s,,tlting out the alkalimetal salt tlius prodliced in sollition; by di55 rectly salting out tb-e Stebbins acid from the solution by the I addition of an alkali-i-netal salt; etc. The following exai-nple illustrates one method of practicing th,e invention. The 60 parts are by -weigilt. Exainple.-220 Farts of 100 per cent. sulfuric acid are cooled to a temperature of about 50 C., aiid 100 parts of betanaphthol in fiiiely divided condition ( 10 mesh or 6,5 silialler) is added wi-th agitation, not more than about 3 minutes being required for the addition. The temperature spontaneously rises to about 20' to 250 C. If after about 8 to 13 ininutes from the completion of the addition of the beta naphthol the batch has 70 not beguii spontaneously to crystallize, a small portioii of crystals of Stebbins acid is added to the reaction mixture. If this shoulcl fail to produce crystallization, ad@ -diti6nal portions are added at 'short inter- 75 vals until crystallization of the Stebbins acid has beeii induced. Sulfonation is allowed to coiitinue for about 30 minutes after the beta-naphthol has all bee-n added, the tem@ perature being maintained at a point not ex- 50 ceeding 300 C., and the iiiass is then mix'ed w@thout delay with about 200 parts of ice while agitatiilg. After substantially the whole stilfoi-iqti6n mixture has.gone into soliition, a small @finount of diatomdeeous earth, 85 such as Filter Cel is added, aiid the mass is filtered with suction to remove any insoluble material present. Common salt (NaCl) is then added to the filtrate to salt out the St6bbins acid, ab6ut 150 parts thereof being re- go qu . ired. The mixture is agitated f or several hours to coinplete the salting out, - is iiltered on a, suction filter at a temperature of about 250 C., and is sucked dry. Stebb'ns aci,d of a superior quality is thus ob- Oci tained in a yield of approximately 95 per c t. of the theoretical, based upon the betaen naphthol employed. It will be realized that the invention is not liii'lited to the process and the details 100 ihereof which are 'set forth in this foregoing sp6cific example. Thus, beta-naphthol of varying grades of piirity may be employed, but it becomes iiiereasinoly difficult with a decrease in the urity @i, the beta-naphthol to io5 induce erl,stallization of the Stebblns acid produced'; and inasmuch as the yield of Stebbins@ acid is greater the sooner crystallization occui-s, the yield of Stebbins acid 'is decreased. The stren(-th of sulfuric acid may 110 iary as above pol'nted out, crystallization, however, also beiiig niore difficult when the weaker acid is used. The amount of acid employed may vary from about 200 to 230 parts, preferably 215 to 220 parts of 98 per 115 cent. to 100 per cent. sulf uric acid per loo parts of beta-naphthol. With weaker sulfuric acid than about 98 per cent the amount of acid employed is decreased in"order to decrease the difficulty in I)roducing crystalliza- 120 tion of the Stebbins acid, but this also decreases -the speed of the reaction, leading to delayed crystallization and a lowered yield of Stebbins acid, aiid requiring a, longer time foi- the completion of the reaction. In seed- 12,5 ing the reactio n mixture, a crystal or crys tals of the free Stebbins acid or of a soluble salt of Stebbins, acid may be used, e. g., the S64i@iin salt of Stebbins 'acid. The sulfonat;lon mixture is preferably prevented from 130