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US653555A - Apparatus for recovering solvents. - Google Patents

Apparatus for recovering solvents.
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US653555A
US653555AUS73320899AUS1899733208AUS653555AUS 653555 AUS653555 AUS 653555AUS 73320899 AUS73320899 AUS 73320899AUS 1899733208 AUS1899733208 AUS 1899733208AUS 653555 AUS653555 AUS 653555A
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Prior art keywords
vapor
chamber
solvent
hat
drying
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US73320899A
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William Beamont Hart
Adam Ashworth
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SOLVENTS RECOVERY Co
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SOLVENTS RECOVERY Co
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Priority to US73320899ApriorityCriticalpatent/US653555A/en
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No. 653,555; Patented .Iuly lo, I900.
W. B. HART & A. 'ASHWORTH.
APPARATUS FOR RECUVERING SDLVENTS.
(Appliqation filed Oct. 10, 1899.) (No Model.) 2 $heetsSheet No fi ax Q1 3- 8 F N ya CO\ I J V 1 L WITNESSES: S INVENTORS WILLIAM B.'HAI?T ADAM A-SHWORTH m: NORRIS PLTERS co. PNOTDLIYNOY. WAsKmG'mN. u. c
Patented July l0, I900. W. B. HART 8L A. ASHWDRTH. APPARATUS FOR BEGOVERING SOLVENTS.
(Application filed Oct. 1Q, 1899.)'
2 Sheets$heet 2.
(No Model.)
U 6 8 s F 1 m 7 H U m 2 w k. 7%
INVENTORS WILL/AM B. HART ADAM AsHwonTH WITNESSES: ?-,U4- Z7 7 THE Noam: PETERS no. PHOYOLITHQ. msmym'cn. nv cv UNITED STAl'rn-sj P TENT --OFFICE.
WILLIAM BEAMONT HART AND AEAM ASHWORTH, OF MANCHESTER, ENG- LAND, ASSIGNORS TO THE SOLVENTS RECOVERY COMPANY, OF SAME PLACE, AND JAMES MARSHALL, OF FALL RIVER, MASSACHUSETTS.
vARMRATUS RI REICO'VE'RING so L;V'E NTS.
SPECIFICATION forming partb f Lett rs rar'lit no; 653,555, 'dated July 10, 1900. Application filed October 10, 599. 'seriaino. 733,208. (in, model.)
To all whom it may concern/.-
HART and ADAM ASHWORTH, subjects of -Victoria, Queen of Great Britain, residing at Manchester, England, have invented certain new and useful Improvements in the Recovery of Solvents from Stiffened Hat Bodies and in the Apparatus Employed Therein; and we do hereby declare the following to be a full,
clear, and exact description of the invention,
such as will enable others skilled in the art to which it appertains to make and use the same. 1
Our invention relates to the recovery of solvents fromhat-bodies that have been stifiened and in the apparatus for eifecting such recovery, and has for its object to obtain the recovered solvent in a strong condition, so
that it can be used repeatedly for further stiifening purposes.
With these ends in view our invention consists in certain methods and in following out certain steps, such as will be hereinafter fully described and then specifically be designated by the claim.
parts in the several figures of the drawings.
In the process'of proofing or stiifening of hard hats the hat-bodies are treated with a solution of shellac or other gums or resin or stiffening material in a solvents'uch as methylated spirit, wood-spirit, &c.-and the solvent then evaporated, 1 1 In apparatus used for the purpose of evaporating and recovering this solvent it has been found that when a solvent is used that is miscible with water such as methylated spirit, wood-spirit, 850.- the recovered spirit is weak and dilute and p after a time it becomes incapable of dissolv- Be it known that we, WILLIAM BEAMONT ing shellac, &c. This dilutionis due to the presence of water in the'hat-b odies, such water being evaporated and condensed with the solvent.
In carrying our invention into effect the proofed hat-bodies while moist are placed in a closed andheated chamber through which hot air circulates. The solvent contained in the hat-bodies is thus evaporated, together with the aqueous moisture, and absorbed by the air and is then carried forward to a solvent-vapor-drying chamber, which can also be heated to prevent condensation of the solvent vaporr I In this solvent-vapor-drying chamber dehydrating or drying material is placedsuch as quicklime, potassium carbonate, or substance of a similar natureby -whichthe aqueous vapor carried over with the solvent-vapor from the hat-body chamber may be arrested, while the heated solventvapor thus dried passeson, stillin vapor form, to a condenser, where it is condensed and separated in liquid form. The cold air from the condenser is returned by an air exhauster, fan, or pump through a heater into the hatbody chamber, this circulation being continued until the operation is finished. The apparatus consists of a hat-body chamber 1, constructed of metal or other suitable material and provided with adoor 2, so arranged that when closed a tight joint is formed, preventing the escape or admission of air or the escape of solvent-vapor. An outlet?) in the upper part of this chamber communicates by the pipe 4 with the solvent-vapor-drying chamber 5, provided with solidimperforate shelves 6, containing dehydrating ,or drying agentssuch as quicklime, potassium carbonate, &c.and which can be heated, as required, by. the steam-casing 7. 0 From this chamber 5 apipe 8 communicates with the condenser 9, constructed of coils of piping or of tubes toobtain efficient condensing-surface and placed inside acasing 10, through which casing a current of cold 5 water flows. The lower end of the condenserpipe 9 is cut off obliquely and enters for a short distance into aseparator 11, which communicates at its lower end by a pipe 12 with thecollecting vessel 13, in which the condensed solvent is collected. Thisseparator 11 also communicates on one side farthest from the oblique end of the condenser-pipe 9 by apipe 14 with the inlet-opening 15 of an air exhaust, fan, orpump 16. Thepipe 14 rises in an upward direction from theseparator 11 for a convenient height and then falls again to the exhauster, so as to prevent any condensed solvent passing forward to the exhauster. The outlet 17 from the exhauster is connected by apipe 18 with a series of heating-pipes 19, in which the return air is heated before its passage into the hat-body chamber at theinlet 20.
Outside and along the front of the hat-body chamber 1 a movable platform ortrolley 21 is arranged to run onwheels 22, preferably on or inrails 23. This platform is constructed level with the floor of the hat-body chamber and carries alight wagon 24 onwheels 25, guided also, preferably, onrails 26. This wagon contains a number of open shelves or supports 27, on which the hat-bodies are placed. On the floor of the hat-body chamber rails 28 are placed, corresponding with the rails on themovable platform 21, so that when the platform is opposite thechamber 1 thewagon 24 can be run from the platform into thechamber 1 or from thechamber 1 onto theplatform 21 and thence to any required place.
Inside the hat-body chamber 1, but arranged so as not to interfere with the circulation, a false roof orguard 29 is hung in order to protect the hat-bodies from any falling drops of solvent, 650., these being conveyed to the sides.
When the hat-bodies are impregnated with the proofing solution, they are placed on the shelves or supports 27 of thewagon 24. The latter then runs by themovable platform 21 into the hat-body chamber 1 and thedoor 2 is secured. By theexhauster 16 the air inclosed in the apparatus is then caused to circulate and is then heated by theheatingpipes 19. The solvent in the hat-bodies then evaporates, and by circulation the hot atmosphere of solvent and aqueous vapors and air is carried through theoutlet 3 and pipe 4 to the heated solvent-vapor-drying chamher 5, where the aqueous vapor is absorbed by the dehydrating or drying agent and so removed. The dried solvent-vapor passes on by the pipe 8-t0 the condenser 9, where the solvent-vapor is cooled and condensed to liquid form, falling through theseparator 11 and pipe 12into thecollecting vessel 13. The air passes forward by theside pipe 14 through theexhauster 16 and pipe 18 into a series of heating-pipes l9 and returns to the hat-body chamber by theinlet 20. This circulation is continued until the operation is finished. this manner one definite volume of air inclosed in the apparatus is caused to circulate through the said apparatus, and to effect the removal of the solvent-vapor through the solvent-vapor-drying chamber, where the solvent-vapor is dried by removal of aqueous vapor into the condenser, where it is condensed and so recovered.
In order that our improvement may be clearly understood as to all its details, we would state more explicitly the manner of carrying out our process.
In our invention we place the hat-bodies, from which we desire to recover the alcohol or other solvent in a strong-condition ready for reuse, in theheated chamber 1, from which chamber (equivalent to a still) the alcohol or other solvent vapor passes in an upward direction into the vapor-dryingchamber 5, which is also heated to the desired temperature as required. In thischamber 5 we place a solid drying agent in a number of trays, the bottoms of which trays are not perforated, but solid. These trays are placed one above the other and arranged in such a manner that the vapor passes fromchamber 1 over the surface of the drying agent in each tray, one after the other in successive order, from the lowest to the highest tray in an upward direction until it leaves thechamber 5 and passes into thepipe 8,1eading to the condenser. The trays containing the solid drying agent are all separate and have no connection with each other. Thus we obtain a very large area of water-vapor-absorption surface, and since in this upward direction the vapor continually meets with fresh or new drying material the water vapor is practically absorbed, while the alcohol or other solvent vapor thus freed from water-vapor passes on bypipe 8 to condenser 9. The drying-charm ber 5 is heated by steam to a higher temperature than the boiling-point of the alcohol or other solvent, so that no condensation of the alcohol or solvent vapor or water-vapor ocours; but the water-vapor is absorbed by and enters into combination with the drying agent used. Th us we have no dropping of liquefied drying agent, no formation of spray, and no solution of the drying agent to treat afterward. If we had any condensation in our apparatus, such condensed liquid would run down intochamber 1, containing the hatbodies, which latter would then be utterly spoiled, especially by the drying agent contained in this condensed liquid. The now- 7 dried alcohol-vapor inpipe 8 passes into the 3,after the vapors have left thechamber 1 and before they reach the chamber 5-and this condensation can only be very slight such condensed liquid is caught by thefalse roof 29 and conveyed to the sides ofchamber 1; but it must be borne in mind that this condensation, if it occurs, occurs before the vapors pass over the drying agent, and being thus condensed they cause no solution of the drying agent. This condensed liquid in falling to lower parts ofchamber 1 is evaporated in evaporation-chamber 1 and passed intochamber 5 and then dried by removal of water-vapor. Therefore our method for the removal of water-vapor from the alcohol or solvent vapor is a dry process, in which we use a dry solid agent for this purpose, not a liquid solution, and we carry this out by passing the vapors over the surface of this drying agent and not through it. We also keep the evaporation operation separate and quite distinct from the water-vapor-absorption operation, yet these two operations proceed simultaneously.
By the fan (also called exhauster) we cause a circulation of the air inclosed in the whole apparatus. It is true we exhaust the atmosphere of air, water-vapor, and solventvapor from the evaporation-chamber, so that we do not reduce or lessen the atmospheric pressure in the evaporation-chamber, nor do we cause the water or the solvent to evaporate at a lower temperature. We only cause these two to evaporate quicker by removing their vapors as fast as they are formed.
It is the water present in the hat-bodies that can cause the dilution of the recovered solvent. The water present in the atmosphere inclosed in the apparatus is only an infinitesimal quantity, and since this same air is confined during the whole operation the quantity of Water in the air can for all practical purposes be neglected.
Any suitable drying agent may be employed which will absorb the aqueous vapor as vapor and which will therefore not become liquefied, the object being to absolutely free the solvent-vapor from water in any form before the condensation of such solvent-vapor takes place; but by experiment we have ascertained that the only drying agents which we can use are anhydrous alkaline carbonates, such as potassium carbonate (K 00 anhydrous alkaline sulphates, such as sodium sulphate (Na SO or anhydrous alkaline-earth oxides,such as quicklime (OaO) in solid form, either in lump or powder.
Any form of apparatus for heating the air may be employed. It is found a convenient plan to place the hat-body chamber inside the hat-stove in general use in hat-works and to heat the air in a series of pipes placed in the stove. This heat may be supplemented by means of a steam-coil 30, arranged inside the lower part of the hat-body chamber.
Asmaller door 31 is fixed on thedoor 2 of the hat-dryingchamber 1, so that the hatbodies may be quickly removed for examination during the operation. This door is also arranged to fit tightly when closed. Numbers of these hat-body chambers may be worked together, the inlets and outlets for vapor and air being controlled by suitable valves. The solvent-vapor-dryingchamber 5 is also pro= Vided with adoor 32 to shut tightly.
Having thus described our invention, what we claim as new, and desire to secure by Let ters Patent, is-- In an'apparatus for recovering the solvents from stifiened hat-bodies, a hat-body-dryingchamber 1, in combination with a series of superposed trays or shelves arranged therein, a tapering outlet from the top of the said chamber, an inclined false roof or guard hung to the under side of the said top and. extending under the said outlet where it is provided with an opening discharging into the same, a drying-chamber into which the said outlet discharges and a condenser communicating with the outlet of the said drying-chamber, substantially as set forth.
In testimony whereof We affix our signatures each in the presence of two witnesses.
WILLIAM BEAMONT HART.v ADAM ASHWORTH.
Witnesses as to the signature of William Beamont Hart:
WILLIAM HENDERSON HAWDON, JAMES KINNACH.
Witnesses as to the signature of Adam Ashworth:
EDWIN ASHWORTH, HARRY BERESFORD.
US73320899A1899-10-101899-10-10Apparatus for recovering solvents.Expired - LifetimeUS653555A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2467435A (en)*1944-08-251949-04-19Anderson Co V DSolvent recovery distillation system
US2480954A (en)*1944-05-061949-09-06Westinghouse Electric CorpDehydration of foods by sublimation
US2499328A (en)*1947-10-151950-02-28Sam Sam WomenApparatus for drying laundry
US2723923A (en)*1947-10-021955-11-15Munters Carl GeorgMethod of impregnating multilayer paper insulation
US5709038A (en)*1993-09-241998-01-20Optimum Air CorporationAutomated air filtration and drying system for waterborne paint and industrial coatings
US6035551A (en)*1993-09-242000-03-14Optimum Air CorporationAutomated air filtration and drying system for waterborne paint and industrial coatings
US6203859B1 (en)1993-09-242001-03-20Optimum Air CorporationMethod of drying substrates and use thereof

Cited By (8)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2480954A (en)*1944-05-061949-09-06Westinghouse Electric CorpDehydration of foods by sublimation
US2467435A (en)*1944-08-251949-04-19Anderson Co V DSolvent recovery distillation system
US2723923A (en)*1947-10-021955-11-15Munters Carl GeorgMethod of impregnating multilayer paper insulation
US2499328A (en)*1947-10-151950-02-28Sam Sam WomenApparatus for drying laundry
US5709038A (en)*1993-09-241998-01-20Optimum Air CorporationAutomated air filtration and drying system for waterborne paint and industrial coatings
US5970625A (en)*1993-09-241999-10-26Optimum Air CorporationAutomated air filtration and drying system for waterborne paint and industrial coatings
US6035551A (en)*1993-09-242000-03-14Optimum Air CorporationAutomated air filtration and drying system for waterborne paint and industrial coatings
US6203859B1 (en)1993-09-242001-03-20Optimum Air CorporationMethod of drying substrates and use thereof

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