US475106A

US475106A - Bridge

Info

Publication number: US475106A
Authority: US
Publication date: 1892-05-17
Anticipated expiration: 1909-05-17

Description

1 (No Model.) 3 Sheets-Sheet 1.

G. L.'P. EYRE & -T. J. HOPKINS. APPARATUS FOR TREATING WOOL 0R LIKE SUBSTANCES.

No. 475,106. 1 Patented May 17, 1892.

(No Model.)

3' Sheets-Sheet 2 G. L. P. EYRE & T. J. HOPKINS. APPARATUS FOR TREATING WOOL OR LIKE SUBSTANCES.

No. 475,106. Patented May 17,1892.

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' s Sheefis-Shet a. G. L. BYR & T. J. HOPKINS APPARATUS FOR TREATING WOOL 0R LIKE SUBSTANCES; 7 No. 475,106. r Patented May 17, 1892.

(No Model.)

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' UNITED STATES PATENT, OFFICE.

GEORGE L. P. EYRE, OF LONDON, AND THOMAS J. HOPKINS, OF 'TROlV- BRIDGE, ENGLAND.

APPARATUS FOR TREATING WOOL OR LIKE SUBSTANCES.

SPECIFICATION forming part. of Letters Patent No. 475,106, dated May 17, 1892. Application filed December 10, 1889. Serial No. 333,297. (No model.) Patented in England December 27, 1888, No. 18,907.

To all whom it may concern:

Be it known that we, GEORGE LEWIS PHIPPS EYRE, solicitor, residing at 1 John Street, Bedford Row, London, in the county of Middlesex, England, and THOMAS J OHN HOPKINS, engineer, residing at Cradle Bridge Vorks, Trowbridge, in the county of Wilts, England, sub jects of the Queen of Great Britain, have invented new and useful Improvements in Apparatus for Treating WVool and Like Substances, (for which we have obtained British Patent No. 18,907, dated December 27, 1888,) of which the following is a specification.

This invention relates principally to the extraction of oil and fat and oily and fatty matters from wool; but it is also equally applicable to the extraction of oily and fatty matters from woolen yarns or fabrics and such other fibrous material or mixtures of materials as are from their nature affected in color or quality, when known agents-such as bisulphide of carbon or similar solvents are used for the purpose of extracting such oily and fatty matters, and are subsequently removed from the material under treatment by the slow process of admitting steam or using other means of raising the temperature to the respective boiling-points of such solvents and so driving them off by evaporation.

The object of this invention is to provide a suitable apparatus whereby oily and fatty matters may be extracted by the use of bisulphide of carbon or similar solvents of. the greasy, oily, or fatty matters without employing heat and so causing injury to the materials operated upon, and by which process and apparatus the fatty matters and the solvent employed are removed from the materials under treatment, the solvent and the vapors given off therefrom being to as large an extent as practicable afterward recovered and used in subsequent operations, thus effecting great economy, while the noxious or poisonous vapors are prevented from escaping into the works or factory where the operation is carried on.

In order that our invention may be more fully understood and carried into practice, we will now proceed to describe the same with reference to the accompanying drawings, in which similar letters and numerals are used to indicate corresponding parts in all the figures.

Figure l is a plan view showing the general arrangement of the different parts of an apparatus embodying our invention. Fig. 2 is a side view or elevation of the intermediate tank B. Fig. 3 is a vertical section through the tank 1), taken on the line 3 3 of Fig. 1. Fig. 4 is an end elevation of the centrifugal machine or apparatus shown in top view in Fig. 1. Fig. 5 is an elevation, on a somewhat larger scale, of the centrifugal apparatus, showing the means for raising and lowering the cover thereof. Fig. 6 is a vertical section through the scrubber on the line y 'g of Fig. 1. vation of the centrifugal apparatus. Fig. 8 is a vertical section, enlarged, of the revolving casing or basket of the centrifugal apparatus. Fig. 9 is a sectional elevation onthe line as a: of Fig. 1 on an enlarged scale. Fig. 10 is a sectional elevation in outline of the Fig. 7 is a vertical sectional elecover of the centrifugal apparatus and through the supply-pipe 1. Fig. 11 is an end elevation of the centrifugal apparatus on an enlarged scale. Fig. 12 is a top plan view of Fig. 11. Fig. 13 is an elevation of the upper part of the centrifugal apparatus, showing the hinge of the cover thereof in front view. Fig. 14 is a sectional elevation of a part of the outer-casing of the centrifugal apparatus.

The revolving cage or basket O of the centrifugal drying-machine is formed with a conical boss D, whereby it can be fixed upon the spindle F in the well-known manner, and which spindle is rotated by any suitable motive power. The cover E of the centrifugal is made preferably of the shape shown in Fig. 7, the dome-shaped center F conforming to the shape of the boss D, so as to economize space and at the same time form a passage way for the air admitted into the machine for the final drying of the material under treatment.

L L is an annular trough around the top of the centrifugal-case for the reception of water, into which the rim M M of the cover is placed, forming the water seal.

In Figs. 10 to 13 are shown the means adopted for supplying a water spray or shower to the material under treatment in the revolving centrifugal-basket while the machine is in motion. Fig. 10 is a sectional elevation of the cover of the machine, and shows the water-supply pipe 1 and the annular perforated spray-producer 2, the inner side of which forms the baffle H. In Figs. 5 and 13 is shown the hollow trunk 3 and the hollow trunnions and hinge 4. Fig. 13 is a' front view of the spray arrangement, showing the gland and stuffing-boxes 5 5 for keeping the trunnions water-tight while acting as a hinge to the centrifugal-cover and the water-supply valve 6. The action of this part of the apparatus is as follows: By opening the valve 6 the water flows into the hollow trunk 3 and continues its course through the hollow trunnions 4, thence through the supply-pipe 1, Fig. 10,into the annular spray-producer 2, ultimately falling in a shower through the perforations in the annular spray-prod ucer provided for that purpose. 'Fig. 5 also shows the friction-hoist for raising and lowering the cover E into and out of position. A suitable chain 7 is attached to the cover and passed over fixed pulleys 8, and its other end attached to a pulley 9, forming part of a friction-clutch 10, actuated by hand. i A pulley 11 is rotated by an endlessband 12, and the hoisting apparatus is brought into gear with the pulley 11- by means of the clutch 10. l

G is the air-valve formed in the center of the dome F, and through which said valve the air-passes into the interior of the cover through the passage-way between the boss D and the dome F, and is deflected by the annular baffle H, thus causing the air to pass down the inside of the reticulated or perforated cage or basket Ct'.e., the side nearest the spindle as indicated by the arrows in Fig. 7.

The basket or revolving part of the centrit'ugal machine is constructed as follows: In Fig. 8 thecrown or dome D D is of caststeel, to which is riveted the cone or body B B. To the bottom of this is riveted the soleplate or bottom ring 0' O, which is riveted to and supports the perforated cylinder 0 O. The upper rim of the cylinder is strengthened by the rim-plate E E and at suitable distances from top to bottom by the hoops or rings 1' 2 3 4E. The cylinder is also lined inside with wire-netting to prevent the escape of the material or materials under treatment through the perforations of the cylinder. The whole of the basket may be made of wrought iron or steel and preferably galvanized. The basket is mounted on the spindle-F, and is secured thereto by the nut G. The whole is underdriven by means of a pulley and belt or any suitable driving-gear. By reason of the centrifugal force developed by the rotating cage or basket the air will escape toward the circumference of the cage and will thoroughly permeate and effectually dry the material in the cage or basket 0 as it passes therethrough. The air thrown off from the circumference as the cage 0 rotates is led by the collectorplate J, fixed upon the interior of the side of the centrifugal machine, through the outlet K (see Figs. 7 and 14 and 11 and 12) and direct to the condenser Q, or through the pipe T, intermediate tank B, and pipec, as shown in Fig. 1. The outlet K ex tendsnearly from the topv to the bottom of the centrifugal and is closed or opened to the condenser Q by means of the stop cook or slide K or any suitable valve communicating with the outlet-tank K which is in connection with the intermediate tank B or with'the condenser Qdirect. The collector-plate is preferably a piece of thin sheet metal bentto the shape shown in Fig. 14 and fixed to the inside of the machine, as shown, andserves to draw the air down and through the material under treatment. The upper part of the centrifugal-case is provided with a displacementpipe N, covered with a shield O, fixed on the inside of the centrifugal-case. leading from the bottom of the recess formed by the shield and discharging outside the case, is also provided. The agent employed is introduced at the bottom of the centrifugalcase A through the pipe 0, from the reservoir A and allowed to rise therein, percolat ing through the reticulated cage or'ba'sket and saturating the material under treatment until it fills the machine, the displaced air or vapor being driven off through the pipe N and led direct to the condenser Q, or through the pipe Tand intermediate tank B and pipe 0, as shown in Fig. 1. Any of the agent passing over the top of the shield Ois carried off by the draining-pipe P and collected in a suitable receiver or led direct by other pipes to a reservoir, from whence it is pumped or otherwise passed into the still orinto the pipe conveying the bulk of the agent from the centrifugal to the said reservoir. When the water is introduced for the purpose of cleansing the material, the action of this part of the apparatus is the same.

R is an ordinary sight-gage on the side of the centrifugal-case. To avoid complication, the pipes leading the agent out of the centrifugal machine, as also the pipes leading the waterv thereinto and the still for evaporating the agent led off from the bottom of the cen-' trifugal after it has saturated the materials under treatment and separated or dissolved the oily or fatty matter contained therein, are not shown in the drawings, as they are of the ordinary construction and will be well understood without illustration. All the inlet and outlet pipes connected to the centrifugal machine are provided with suitable shut-off valves, which are manipulated according to the stage of the process.

In Figs. 1, 2, 3, 6, and 9 we have shown the means adopted for condensing the vaporized agent evolved during the process and passing off through the displacement-pipe N. The cleansing-water is run off from the centrifugal through the pipes S and T into the intermediate tank B, (see Figs. 1 and 2,) from A pipe P,

IIO

whence it passes through the pipe U into the catch-tank W. The bottom of this intermediate tank B is below the level of the pipe T, as shown in the elevation, Fig. 2, for the purpose of checking the rush of the water from the centrifugal and also to allow the agent to sink to the bottom, from whence it is carried into the catch-tank W by the pipe U before the water contained in the intermediate tank. This pipe U discharges at the bottom of the said catch-tank, so that the contents of the intermediate tank will be deposited at the bottom of the catch-tank, the water, by reasonof its less specific gravity, rising to the top. I The overflow of water fromthe catch-tank may or may'not be carried by the pipe a, into the final tank b, fitted with any suitable number of vertical diaphragms or partitions b, alternately open at the bottom and top, as shown in Fig. 3, and beneath and over which partitions the water passes and in so doingdeposits the potash and other insoluble matters held in suspension and carried off with the cleansing-water from the wool or other material under treatment to be afterward dealt with. The displaced air and vapor given oif in the process is carried by the pipes N and T through the intermediate tank B, from whence itpasses by the pipe 0, turned up at right angles to the intermediate tank B, as shown in Fig. 2, into the condenser Q, which consists of ordinary sinuous or coiled tubes surrounded by water. A pipe cl is connected to the end of the condensing-tubes for the purpose of carrying off the agent, which has been liquefied, and discharging the same into the bottom of the catch-tank V. The remaining vaporized agentis drawn through thebraneh pipe e into the tank or receptacle fby meansof the exhausting-fang (see Figs. 1 and 9) working therein. This fan is driven by a band passing over the pulley 0' or by any suitable motor. The tank or receptacle f is provided with a pipe 71, through which the liquefied agent passes into the catch-tank NV. The remainder of the vaporized agent passes through the pipe j to the scrubber-tank It. The vapor is here met by a spray of cold water issuing through the nozzle at the end of the pipe '6, taken from the Deane pump, as shown at m and n, Fig. l or this may be taken from any water-supply. The water and the liquefied vapor are then carried off by the pipe p to the catch-tank. The remaining uncondensed vapor, if any, is now allowed to pass by the uptake q above the roof of the building, a steam-jet a being provided, if necessary, to facilitate the discharge.

In operating our improved apparatus we place the material to be treated in the cage or basket of the centrifugal or in smaller cages or baskets placed therein, and the cover being adjusted carbon bisulphide or similar solvent (hereinbefore designated as the agent) is admitted through suitable pipes leading into the top side or bottom of the outer case of the machine until the machine is filled,

off, the cage or basket is revolved so asto throw off from the material as much as possible of the oily and fatty matters andthe agent mixed therewith, which runs into the aforementioned reservoir or tank, and from thence the resulting liquid is pumped into the tank A, situated above the centrifugal, to be used again in subsequentoperations untilsupersaturated with such oilyand fatty matters, when it is pumped into or otherwise passed into a still. Here heat is applied, preferably by a steamcoil pipe or steam-jacket, and the agent recovered by distillation by means of suitable distilling apparatus in the ordinary manner, leaving the oily and fatty matter in the still to be afterward dealt with. When the mixed agent and oily and fatty matters have run off from the centrifugal machine, water under pressure or otherwise is admitted into the machine in the same manner as the agent for the purpose of cleansing the material and of washing out any agent or mixed agent and oily and fatty matters which may remain in the material under treatment, and the resulting liquid is allowed to run off in an intermediate tank, where the agent falls by its gravity to the bottom and is carried 0E by a pipe into a final catch-tank. After this resulting liquid has run off the revolving basket is again set in motion, and then water is admitted to'the inside of the centrifugal through the spray arrangement, Which is fixed to the inside of the lid or cover for the purpose of aiding in the dispelling of any remaining agent from the material under treatment, and at the same time it condenses the vapor formed in the centrifugal While in motion, leaving the machine by the outlet, which is closed or opened by means of the stop-cock provided for that purpose on the side of the casing and communicating with the intermediate tank last aforesaid, and when the spray has been sufficiently applied it is turned off, and the revolving basket continues in action until the material is sufficiently dry. To assist this last operation, a fan or blower may be employed or other suitable means may be adopted for producing a current of air. During the process the displaced air and any vapor given off by the agent and the air used in drying are led by suitable pipes or tubes either through the intermediate tank last referred to or to a condensing apparatus, the uncondensed residue being drawn by a fan Working Within a tank or by an exhauster to a scrubber or receptacle, into which a jet or spray of water is discharged, so as to throw down any remaining vaporized agent.

The remainder of the vapor being now practically free from the agent passes into an uptake or chimney, discharging into the open air above the building, the discharge being facilitated by a steamjet or similar means, if found necessary. The condenser-fan and scrubber discharge the recovered agent into the catch-tank. 1

All the reservoirs or tanks used for the storageor reception of the agent are preferably constructed with manholes and hermeticallysealed covers, and each opens into a ventpipe carried above the roof of thebnilding to lead off the air displaced from the tanks by the entry of the agent therein.

As a further mode of recovering any of the agent which may be left in the wool or other material after it is removed from the centrifugal machine into the washing-machine, an automatic agent separator or trap is affixed to or communicates with the outlet-pipe of the washing-machine, so as to carry olt the agent, which by its greater specific gravity separates itself from the water in its passage from the washing-machine. This trap consists of a pipe or casing with a longitudinal diaphragm from side to side for a part of its length, with an outlet-pipe above and below the diaphragm at one end and an inlet-pipe at the other end.

This invention and arrangement of mechanism or machinery herein described can also be applied to fabrics or other materials containing greasy matters for the purposes indi-' cated, in-combination with the employment of agents other than bisulphide of' carbon, but having the same'or analogous properties.

What we claim is' 1. In a machine or apparatus for the treating of wool and like substances, the combination of a centrifugal device consisting of a revolving perforated cage or basket, the surrounding casing having the outlet K, and the collecting-plate J for directing the air thrown off by the centrifugal action of the revolving cage or basket into such outlet, substantially as described.

2. In a machineor apparatus for the treating of .WOOl and like substances, the combi-.

nation, with a centrifugal device, of a casing therefor having a cover provided with a valved air-opening,a battling-plate I-I, surrounding such opening, a spray-producing device ar ranged outside of andadjacent to the said baffling-plate, and a fluid-supply pipe leading to the said spray-producing device, substantially as described.

3. In a machine or apparatus for treating Wool and the like, the combination, with a centrifugal device, of a casing surroundingit, a cover therefor, a hollow liquid-tight hinge for the cover, a liquid-supply pipe leading to this hinge, and a liquid-pipe leading from the hinge-into the said casing, substantially as described.

4. In an apparatus for the treating of wool and the like with a solvent agent, the combination of a closed casing in which the wool is treated, an exit-pipe therefrom for the liquid with which the wool is treated, the intermediate tank B, into which the said exit-pipe en,-

ters above the level of its bottom to facilitate the settling therein of theagent, the pipe W, leading from the bottom of such tank, through which the settled agent may be drawn otfland another pipe 0. leading from the up.- per portion of the said tank to a condensing apparatus, substantially as described.

. G. L. P. EYRE.

THOMAS J. HOPKINS.

Witnesses to the signature of George Lewis 153 St. John Street Road, London.

Witnesses to the signature of Thomas John Hopkins:

W. WALBY, Market House, Trowbrtdge, House Agent.

JOHN HENRY BATTS, Trowbrtdge, Timber Dealer.