USRE5351E - Improvement in bxstltlingturpentiney - Google Patents

Improvement in bxstltlingturpentiney Download PDF

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USRE5351E
USRE5351E US RE5351 E USRE5351 E US RE5351E
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pipe
chamber
still
separator
turpentine
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  • V ⁇ supplyring .tl:lenecessary heat to' liquidizefthe crude material...
  • L'My ⁇ improvec ment l also. consistsI lin?'surroundingthe' lower furnace,
  • My-Y-improvemet also consists ini. connecting a separator, 'constrictedas'fherefi inafter'- described-, with a vessel 'lso arranged.
  • Vcha ractl'enlfimprovement also consists inaconveyingthe turpentine from,a the 'conde-userv to ya'clfosej vesf ,s sel, 'sofarran ged-'as 'tol' secure. the /entire s pai ration therefroino'f all: condensed ste/'a in then passing the ftrpentinef to The'sreawdivantage'cf vesselsfinv connection with the :Icon
  • this'aangenaam-j denser isvtlie still which is constructed out of any suitable material, and at its lower section or base is of a concave or circular form.
  • VVithin the vaporizing-chamber of the still B is arranged au ordinary coil, B',l and around the outer curved surface of thestill is a jacket, C,
  • I is a chamber, and is divided into two compartments, the upper one, D1, b eing a liquidizing'- chamber, into which, by means oi a man-hole, D2, the,crudeturpentine is supplied, and the lower one, E, ⁇ bei ng ya reservoir, into which the crude turpentne, after being sutlicentlyliquidf ized, is allowed to pass" by means of the valve D, which yis opened and closed at pleasure by the valve-rod and lever D?.
  • valve E1 From this reserv voir E, by means ofthe valve E1 andjacketed pipe E2,th' e lquillized crude turpent-ine is fed, as occasion may require, tothe eva'poratingf chamber of the still B.
  • This valve E1 is operated'so as to be opened and closed at pleasure, by means ot' a valve-rod and lever, E3.
  • the liquidizing-chamber D1 is secured, on a vertical shaft, F1, the rake or stirrer F.
  • the shaft is secured so as torevolve freely in suitablelbearings on the upperand lowersurfaces of ⁇ the'chamber and atthe centers .theref of, while ythe rake or stirrer F is constructed of any suitable ⁇ material', and is lof the form clearly 'shown'on the drawing.
  • a perforated coil, Ffwhieh isv designed to emit jets of steamthro'ugh the mass of crude turpentine,
  • panded joint, 12 which receives any heavy.
  • This receptacle'M ina-certain sense, also really acts as an additional 'sepa rator, as in this vessel the steam 'which may have remained with the vapor and been con.- densed in the wrm is separated from the turpentine and'drawn oft' at pleasure by1neans ⁇ - of the cock M2.
  • thermometer which it is drawn ofi'4 for barreling by" means of thecock-NZ.
  • a thermometer O, and a proof-stick, O and from thercenterot" itsy concave section, and passing thrrmgh the steam-jacket (.l, leads a pipe, l?, which is provided with' stop-cock, P1.
  • K is a receptacle
  • the turpentine is conveyed y v to the vessel N by means-of the pipe N1, from The still B is provided with,
  • F2 is a sliding valve, which is operated ⁇ by means of a rod and lever, P?. This valve P2 permits the operator at pleasureto open orv fr the mpcration't cent.
  • ipesO2 03,'vvhen the same are combined as t showband arranged in connection with a sui tablefurnace to operate substantially as de# scribed.

Description

Heissued April 15,1823.'
,. WLM/Leases.
UNITED STATES e'fle-TE.NT OFFICE? 7 :+A-'Rosmalen K... ricerca 'l iMPRvE-MNT- lm bllisrngl-.ineTURPENTINE; j s
spbiiicatn omiiiig'part @1f-Letters Patent No. 131,550, ama september ai, 1ere; reissue NG.' 5,3571', Adined 'Semilla-1873; appliaiiosleaerfilSfiere'-I' Beit known that I, ARCHIBALD K. Immof Galveston, Vin the county'of Galveston and Stateiof Texas, did inventv certain Anew and useful Improvements ,inApparatus for vDistillirxg',A Turpentine, 4on Vwhich Letters Patent of :the United States, were granted bearinrv date September V24,' 18.72, and numbered 131,.- 55O5`and that the following; is a lfull,clear,
' and ,exact fdescripti'onof said invention, reference being had to.. the accompanying draw-r ingandthe letters of reference marked there onfmaking part of Athis specification, Ain which -is represented a'vertical. sectional view of my apparatus.. i v The-object jof my-inventi0n;.consis'ts in so constructing the` apparatus'v as to permit of a continuous distillation, orin so .arranging the Y apparatus that so soon as the crude turpentine isiliqu'idized it` isI conveyedto a suitable ch am-V ber, and from. ,which itis aty pleasure fed to the still, thus permitting each and ever;T stage; oi' the processofdistillation. beingcarried onv inthe apparatus at ione andthe same time,
thestill evaporatin g the crude ,turpenti'ne fed from ,the intermediate chamber or reservoir While the liquidiing-chamber r is-V preparing a fresh supply..` The liquidizin gechamber, reser voir, and still are connected by meansof valves and. a jacketed pipe in such-'ma'unerthat -th'e-4 contentsofthe one are readily fed to the" other, asoccasion requires, whichfinsures an un u in tf arruptedk action' ofthe apparatus through-l .out:the.different stagesof the process of dis.
tillation., .My improvement 'also 'consistsin soarrangingand securing pipe in comicotion with thesteamcoil ofthe :still ezmdftheA reservpirl and. liquidizing -chamber :that theV steam which-aids inltheY evaporation of the crude liquidized-turpentine shall servegtopre serve ithe desired and, uniform temperature 'iu thejinterniediate chamber andjreservoir',1and
also faidfin V`supplyring=.tl:lenecessary heat to' liquidizefthe crude material... L'My` improvec ment lalso. consistsI lin?'surroundingthe' lower furnace,
close vessel, froml whichiy isbarreled.
same shall so act on the jacket itself-as to can-se the steam in its passage through the chamber 'which the j acket forms, andlasitpasses. around the lower section ofthe still, to become super- ,heated l My improvement also consists -i-nsur-V rounding the interior wall of the liquidizing'- chamber ywithaperforated coil, and vin provid-` in g .the same vwitha revolvingraskez or stirrer,
which is voperated through a vertical shafthaving its bear-ings at the center of said-chamf ber.` Practicalexperiencehas shown that the continued agitation of the mass 'in connection withthe jets ofsteani Vfrom the perforated coil-and. the heat communicated fromthe coil ofthe still .combined insure the most rapid liquidization= of the .mass ofl crude lmaterlaL My invention also consists inv connectingA the still and' liquidationvchamber veach with the separatorfby means of ipipes,which= lead, re- Spect-iVcly, -fromth'e upperwsection otthese vessels-to 'the lower section -of the separator, and'which permits the vapor-,fas rapidlyas it is generated` in Aeither ofk the vessels, bein g.
conveyed "immediately to `theQ ;separator,' andy alsol in providing" the pipe the still :with an egg or expande receives the'heaver liquid partiell sjwhich may be thrown o from the'. evaporating-chamber of the-still. My-Y-improvemetalso consists ini. connecting a separator, 'constrictedas'fherefi inafter'- described-, with a vessel 'lso arranged. as to receive .the "pyrolg'neousacid `water and f other impurities as they areseparatedlfrom u the vaporizfed materiaLths 'savingthe 4same and providing anarticle off commerce hereto-.l
forewa'sted in-de'vices of this Vcha ractl'enlfimprovement also consists inaconveyingthe turpentine from,a the 'conde-userv to ya'clfosej vesf ,s sel, 'sofarran ged-'as 'tol' secure. the /entire s pai ration therefroino'f all: condensed ste/'a in then passing the ftrpentinef to The'sreawdivantage'cf vesselsfinv connection with the :Icon
ether'. this'aangenaam-j denser isvtlie still, which is constructed out of any suitable material, and at its lower section or base is of a concave or circular form. VVithin the vaporizing-chamber of the still B is arranged au ordinary coil, B',l and around the outer curved surface of thestill is a jacket, C,
which is so arranged in connection therewith as to leave or furnish a superheating steamchamber, C1. Steam from a boiler suitably arranged is, by means of the pipe (l2, supplied to this chamber G1, and after passing under and around the lower section ofthe. still B gy means ot the pipe U3 is conveyed tothe coil By rcicrcnce to the drawing it will be seen that,y in consequence otzmy arrangement of the still B and jacket (l in connection with the fire-pot of the furnace, while the jacket entirely protects the still-B from the direct action of the heat, yet the same is itself so` acted on as tofinsnre the super-heating of. all steam. admitted through'the pipe (32 as it passeslhrough the chamber (31, and,y consequently, under and in direct contact with the still 'B,in which superheated condition through the pipe Cs it is fed to the coil B. I) isa chamber, and is divided into two compartments, the upper one, D1, b eing a liquidizing'- chamber, into which, by means oi a man-hole, D2, the,crudeturpentine is supplied, and the lower one, E,`bei ng ya reservoir, into which the crude turpentne, after being sutlicentlyliquidf ized, is allowed to pass" by means of the valve D, which yis opened and closed at pleasure by the valve-rod and lever D?. From this reserv voir E, by means ofthe valve E1 andjacketed pipe E2,th' e lquillized crude turpent-ine is fed, as occasion may require, tothe eva'poratingf chamber of the still B. This valve E1 is operated'so as to be opened and closed at pleasure, by means ot' a valve-rod and lever, E3.
N'Yithin the liquidizing-chamber D1 is secured, on a vertical shaft, F1, the rake or stirrer F. The shaft is secured so as torevolve freely in suitablelbearings on the upperand lowersurfaces of `the'chamber and atthe centers .theref of, while ythe rake or stirrer F is constructed of any suitable` material', and is lof the form clearly 'shown'on the drawing. Around the interior wall of this chamber D1 is a perforated coil, Ffwhieh isv designed to emit jets of steamthro'ugh the mass of crude turpentine,
it aids in liquidizing the crude inaterial.-l The sections of this pipe" Gr, which arewithiuthe reservoir E andchamb erl)1, are perforated, as "clearlyf's-hown at G1 G?, "H iS lib separator, and consists cfa 'column' hay? series ctraysforpartitions 'E1 H1, having cpr-.nin gs" at vtheir centers, over which are dedectingcaps Hz H2. Immediately below these caps are openings or orifices leading into the inte-4 rior chamber of the separator, which allow of the free passage of all the products of evaporization which are driven into the separator.`
Through an opening infeach of the trays H1- H1 is secured a pipe, H1, the upperv section of which is immediately below the orificev through which the caps H2 H2 deflect the vapors, acid,
`&c. At the upper section of the still B and.
panded joint, 12, which receives any heavy.
liquid particles'which may be driven'with the vapor from the still. T he chamber which this expanded joint forms is emptied at pleasure by `means 'of the stop-cock I3. whichis connected with the separator by m eans of the pipeK1, and into which the pyrolig- -neous-acid water, which is thrown otf'fromthe vapor in its passage through the'separator, is collectedins'tead of being wasted, as heretoforehas been the practice.. From the center of thesdome of the separator leads a pipe, L, which communicates directly with the condensing- Worm L1, and which is ot' ordinary construction, and iucased in a water-tight tank or vessel, L2, in the usual manner." The worm L1 is kept constantly immersedinv fresh v water by means ot1 the supply-pipe LgfAs. the water becomes heated it rises, and is d is- From the worm L1 the condensed vapor'or turpentine is led to aireceptacle, M, bymeans of a pipe, M1, which Y enters the receptacle M at' the lower section.
charged through the pipe L4.
of the same. This receptacle'M, ina-certain sense, also really acts as an additional 'sepa rator, as in this vessel the steam 'which may have remained with the vapor and been con.- densed in the wrm is separated from the turpentine and'drawn oft' at pleasure by1neans`- of the cock M2.
which it is drawn ofi'4 for barreling by" means of thecock-NZ. a thermometer, O, and a proof-stick, O and from thercenterot" itsy concave section, and passing thrrmgh the steam-jacket (.l, leads a pipe, l?, which is provided with' stop-cock, P1.
shut oft' the communication between thestill Ajand thepipe P; ,Through this pipe 1?y the resin in a liquid condition is drawn-'ott'.-intc the strainer R, and thence tothe resinboXlt. y Y
The various featuresot' this apparatus-. are
supported or sustained on' any suitable-framef i? WOiflL Fremthc foregoia :inscri g1 i.
K is a receptacle, i
The turpentine is conveyed y v to the vessel N by means-of the pipe N1, from The still B is provided with,
F2 is a sliding valve, which is operated` by means of a rod and lever, P?. This valve P2 permits the operator at pleasureto open orv fr the mpcration't cent.
a( the apparatus will be readily understood. 'lhe crude material is poured into the chamber D1, and steam is supplied to the perforated coil F2. Motion is then imparted to the shaft F1, which revolves rapidly the rake or stirrer F. This rapid agitation of the mass by the rake, in connection with the jetsof steam and the heatffrom the section G2 of the pipe G, in a at the desired temperatureby means ofthe section G1 of the pipe G. Thecoil B1 i-s `con-v tinually supplied'with superheated steam .from the chamber C1. The valveV E1is now. opened by means of the valve-rod; and-'1e verE 3, and through the jacketed pipe E is su-'ppli'edto the still Bthe llipiidizedturpentine, r--tvfhere,
- at an exceedingly'low temperature, its evaporization is insured. By means off-the y'steam-4 chamber O1, coil B1, and the 'lower 'section of the pipe G, as rapidly -as the evaporization takes place the vapor is fed, by means cffthe pipe I, to the separator H, as visalso any vapor which may be generated in the-liquidiz'- ing-chamber D1,'by means of the pipe l1. En-
tering the chamber of theseparator, it passes up through the opening in the lowertray H1, and, striking against the cap H2, is deflected and escapes by the or-ilice immediatelybelow the cap again out into the chamber and up through the next, and so on throughout the entire series. But in the passage of the vapor through each of thse partitions .or trays H1 and "under the deflectors Ilz it is robbed of more or less of .its` pyroligneous-y acid water, and other impurities, which, being heavier than the vapor, falls and accumulates on theptrays, while the vapor continues its as- But this acid wat-er and the other impurities canonly accumulate to a certain depth, because so 4soon as they reach a point ushwith-.th'e upper openings of the pipes Hf H theybegi to flow down from one tray to another 'untilthey reach. the bottom of the separator H, fromwhich they are conveyed by the pipe` K1 tothe vessel K, to be drawn odas-wanted by means of the cock K2. vThe vaponthusnow comparatively free from vthe acid ater, is conveyed by the pipe L to the wenn .'L1, where its condensation Vtakes place. Butin the process of condensation of the turpentineconsiderable steam or moisture has also been condensed, of which it is most `dei siable to free the v turpentine, therefore, from-- the Worm L1 the turpentine and condensed steam are conveyed together to the vessel M by means of the pipe M1, which pipe'enters at the llowersection of the vessel. The water, being heavier than the turpentine, remains at the bottom, and the turpentine rises until it reaches the opening through which enters the pipe'N1, by which pipe, in a pure. state,'the
turpen'tine is conveyed to the vessel N, and
from which it is drawnoff into barrels. The liquid resin from the still, thepyroligneous acid Water from the vessel K, and the condensed Water from-'the vessel are all drawn oil, as clearlyfshown. o
From the foregoing description it will readily bei seen that each and everystage of the v process is carried on in the apparatus at one and the same time.
What 1 claim as new, anddesire to secure by Letters vPatent of the United States, isl. The' still B, closed coil B', jacket C, and
ipesO2 03,'vvhen the same are combined as t showband arranged in connection with a sui tablefurnace to operate substantially as de# scribed.
2.' VIn combination with the coil B, the pipe G, the same being-arrangedto'operate in connection Withy `thestill 1B, reservoir E, and liquidizi-ng chamber I"D1, substantially as described.
3. The liquidizingfchamber D1,J anfing its interior wall surrounded with, a 'perforated coil, E2, and the revolving rakejF, when the sameareso combined and arranged as to operate substantially asdescribed. o
'4. The chamberl D1, reservoir E, stilll B, valves D3 and E1, and the j'acketed pipe E2, the whole being constructed and arranged to operate substantially as described. i
5. -The vaporpipe I, having an expanded joint, 12, and cock I3,`When the same is connected withthe still and separator ini-such manner as to operate substantiallyL-la's described. l
6, The separator H, vessel K condensingworm L1, pipes L K1, the same being so con,- structed, combined, and arranged asto operate substantially as described.
7. The condensing-Worm L1, vessels M N,
and pipes M1 N 1, the same being soconstruc'ted, combined, and arranged as to operate substantially as described.
In testimony Whereof'Ihave signed my name to this specification before two subscribing witnesses.`
' ARCHIBALD K. LEE.
. Witnesses: l I
EDWIN JAMES, Jos. T. K. PLANT.

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