US2543198A

US2543198A - Mixing apparatus

Info

Publication number: US2543198A
Application number: US69318A
Authority: US
Inventors: Plunguian Mark; Jesse L Riley
Original assignee: Celanese Corp
Current assignee: Celanese Corp
Priority date: 1949-01-05
Filing date: 1949-01-05
Publication date: 1951-02-27
Anticipated expiration: 1968-02-27

Description

M. PLUNGUIAN ETAL MIXING APPARATUS Febo 27, 1951 Filed Jan. 5, 1949 JNVENTORS MARK PLUNGUIAN JESSE L .R|| EY. BY o 'raiented Feb. 27, 1951 UNITED STATES PATENT OFFICE MmNG APPARATUS Mark Pllumlian, Gilette, and Jesse L. Riley, East Orange, N. J., assignors to Celanese Corporation of America, a corporation oi' Delaware Application J anuary 5, 1949, Serial No. 69,318

' 4 Claims. l

This invention relates to mixing apparatus. and relates more particularly to mixing apparatus adapted for the pretreatment of cellulosic material.

In the production of organic acid esters of cellulose, cellulosic material is usually esteritled with an organic acid anhydride in the presence of an esterirlcation catalyst and an organic acid which acts as a solvent for the cellulose ester, forming a viscous solution or dope. It has been customary to pretreat the cellulosic material before esterication to render said material more reactive during the esterification step. In the copending application of Seymour et al., Serial No. 58,028, led November 2, 1948 there is disclosed a two-stage process for pretreating cellulosic material which materially reduces the time necessary for said pretreatment and renders the cellulosic material more highly reactive. As disclosed in said co-pending application, the cellulosic maferial is treated with a lower aliphatic acid during the rst stage of the pretreatment and, durin the second stage of the pretreatment the cellulosic material is treated with an additional quantity of a lower aliphatic acid containing a relatively high concentration oi an esteriiication catalyst such as sulfuric acid.

During the pretreatment, the pretreating agents must be so distributed as to reach all of the cellulosic material, since any cellulosic material which is not pretreated will remain unesteried during the subsequent esterication producing a cloudy dope. It is also important in carrying out the pretreatment process to limit the period of time during which the cellulosic material is left in contact with the pretreating agent applied during the second stage of the pretreatment, since the high concentration of esterication catalyst in said agent has a strong degradative eiect on the cellulosic material. In certain cases it may be desirable to allow a short interval of time to elapse between the iirst and second stages of the pretreatment to permit the pretreating agent applied during the first stage to diffuse through and into the cellulosic material.

It is an important object of this invention to provide a mixing apparatus for pretreating cellulosic material in accordance with the process disclosed in the said co-pending application, which will be especially simple in construction and efficient in operation.

A further object of this invention is to provide a mixing apparatus in which cellulosic materlal may be continuously subjected to a twostage pretreatment.

Another object of this invention is the provision of a mixing apparatus in which a material may be continuously mixed and in which said material may be treated with a fluid agent.

Other objects of this invention, together with certain details of construction and combinations oi' parts, will be apparent from the following detailed description and claims.

In accordance with our invention, we provide a mixing apparatus having a cylindrical shell through which the cellulosic material is fed by means of a helical conveyor. Nozzles are provided at spaced points on the shell for spraying the cellulosic material with the pretreating agents during its passage therethrough, whereby upon leaving the shell the cellulosic material may be esterifled without further pretreatment. The helical conveyor has a large number of turns per unit length in the vicinity of the nozzles through which the pretreating agents are applied than at points spaced therefrom. Because of this variation in the number of turns per unit length, the conveyor moves the cellulosic material past the nozzles at a relatively slow rate permitting the application of large quantities of pretreating agents from a small number of nozzles. This effectively reduces not only the number of nozzles, but also the total required length of the mixer.

The helical conveyor, in addition to moving the cellulosic material through the cylindrical shell, serves to distribute the pretreating agents so as to reach all of the cellulosic material. The efficiency with which such distribution is eiected is higher at those points where the helical conveyor has a lower number of turns per unit length, since the cellulosic material is moved forward more rapidly at those points and the loading of the cellulosic material per unit length of the mixer is thereby reduced. By holding the clearance between the conveyor and the entire periphery of the cylindrical shell at a minimum, the opportunity for any of the cellulosic material to pass through the cylindrical shell without being pretreated is substantially prevented. Similarly, there will be no opportunity for any of the pretreated cellulosic material to remain in the cylindrical shell and become degraded which would affect the properties of the dope unfavorably. To obtain an adequate distribution of the pretreating agents through the cellulosic material, it is preferred that the helical conveyor be operated at speeds ranging from 400 to 1200 R. P. M., or

more. The cylindrical shell may be tilted from the horizontal to permit the throughput of the cellulosic material to be varied over a wide range without changing the speed of the helical conveyor or lessen the efficiency with which said conveyor distributes the pretreating agents through the cellulosic material.

A preferred embodiment of our invention is illustrated in the accompanying drawing in which the figure is a side elevation of a mixer embodying this invention.

Referring now to the drawing, the reference numeral designates a cylindrical shell, which opens at one end into a feed hopper I2 having a hinged cover I3 and at the other end into a discharge hopper I4. A shaft I5 journalled in bearings I 6 and IT, extends through the cylindrical shell and the feed hopper I2, and is driven at any desired speed by the motor I8 through the pulleys I9 and 2| and the belt 22. A screw conveyor 23 is fastened to the shaft I5 in the feed hopper I2 and serves to feed the cellulosic material in said hopper into the cylindrical shell I I. As the cellulosic material enters said shell, it is drawn forward by means of the helical conveyor 24 which is fastened to the shaft I5 with rods 25 that also serve to agitate the 'cellulosic material. A pretreating agent from any suitable source (not shown) is supplied under pressure to a nozzle 26 through a conduit 2l, the said nozzle spraying the pretreating agent onto the cellulosic material. After leaving the vicinity of the nozzle 26, the cellulosic material is moved forward by means of a helical conveyor 28 which is fastened to the shaft I5 by means of rods 29. The helical conveyor 24 is constructed so as to have a larger number of turns per unit length than the helical conveyor 28, as a result of which the cellulosic material is moved past the nozzle 26 at a relatively slow rate, and after passing said nozzle is moved forward at a relatively faster rate.

The helical conveyor 28 feeds the cellulosic material to a helical conveyor 3| that is fastened to the shaft I5 with rods 32. The conveyor 3| moves the cellulosic material past a nozzle 33 to which a pretreating agent from a suitable source (not shown) is supplied under pressure through a conduit 34. The helical conveyor 3|,

like the helical conveyor 24 has a larger number of turns per unit length as a result of which the cellulosic material remains in the vicinity of the nozzle 33 for a relatively long period of time. From the conveyor 3|, the cellulosic material passes to a helical conveyor 35 that is fastened to the shaft I4 with rods 36. The helical conveyor 35 has a small number of turns per unit length and moves the cellulosic material rapidly to the discharge hopper I4.

The cylindrical shell I I is fastened to a framework 31 which is mounted for pivotal movement on a shaft 38 carried by a base 39. A framework 4I depends from the framework 31 and serves to support the motor I8 at a xed distance from the cylindrical shell II. The cylindrical shell |I may be inclined to the horizontal by rotating the framework 31 about the shaft 38 to any desired position, and may be fastened in said position by means of the chain 42 which engages a pin 43. By tilting the cylindrical shell II so that the discharge hopper I4 is positioned above the feed hopper |2, the passage of the cellulosic material through said shell will be retarded; whereas by tilting the cylindrical shell I2 so that the discharge hopper I4 is positioned below the feed hopper I2, the passage of the cellulosic material through said shell will be accelerated.

During operation, thc feed hopper I 2 is charged with a mass of cellulosic material which is fed to the cylindrical shell by means of the screw conveyor 23. As the cellulosic material enters the cylindrical shell II it is sprayed with a pretreating agent from the nozzle 26 and is moved forward and thoroughly agitated by the helical conveyor 24. The cellulosic material then passes to the helical conveyor 28 which agitates it further and moves it along the cylindrical shell II to the helical conveyor 3| and the nozzle 33. During the passage of the cellulosic material to the nozzle 33, the pretreating agent applied from the nozzle 26 diffuses through and into the cellulosic material. As the cellulosic material is drawn past the nozzle 33 it is again sprayed with a pretreating agent, and it is thoroughly agitated by the helical conveyor 3|. The cellulosic material then passes to the helical conveyor 35 which agitates it further and moves it to the discharge hopper I4. After being discharged, the cellulosic material may be esteried directly without further pretreatment.

Although the mixer of this invention has been described with particular reference to the twostage pretreatment of cellulosic material to which it is especially adapted, it may also be employed for other purposes.

It is to be understood that the foregoing detailed description is given merely by way of illustration and that many variations may be made therein without departing from the spirit of our invention.

Having described our invention, what we desire to secure by Letters Patent is:

l. A mixing apparatus comprising a shell, a rotatable shaft in said shell, a conveyor on said shaft for rotation therewith for simultaneously agitating and moving material through said shell, said conveyor comprising a plurality of helices mounted on said shaft in such relation that helices having a relatively large number of turnr per inch alternate with helices having a smaller number of turns per inch, and means in said shell adjacent to the helices having a relatively large number of turns per inch for supplying iluid to the material passing through said shell, the construction and arrangement being such that the material is moved through the shell by the helices having a large number of turns per inch at a slower rate than by the helices having a small number of turns per inch.

2. A mixing apparatus comprising a shell, a rotatable shaft in said shell, a conveyor on said shaft for rotation therewith for simultaneously agitating and moving material through said shell, said conveyor comprising a plurality of helices mounted on said shaft in such relation that helices having a relatively large number of turns per inch alternate with helices having a smaller number of turns per inch, and nozzles in said shell adjacent to the helices having a relatively large number of turns per inch for spraying fluid on to the material passing through said shell, the construction and arrangement being such that the material is moved through the shell by the helices having a large number of turns per inch at a slower rate than by the helices having a small number of turns per inch.

3. A mixing apparatus comprising a shell, a rotatable shaft in said shell, a conveyor on said shaft for rotation therewith for simultaneously agitating and moving material through said shell,

said conveyor comprising a plurality of helices mounted on said shaft in such relation that helices having a relatively large number of turns per inch alternate with helices having a smaller number of turns per inch, nozzles in said shell adjacent to the helices having a relatively large number of turns per inch for spraying iiuid on to the material passing through said shell, and means for tilting said shell from the horizontal whereby the throughput of the material through said shell may be varied without changing the speed of said conveyor, the construction and arrangement being such that the material is moved through the shell by the helices having a large number of turns per inch at a slower rate than by the helices having a small number of turns per inch.

4. A mixing apparatus comprising a hopper, a shell adjacent to said hopper for receiving material therefrom, means in said hopper for supplying material to said shell, a rotatable shaft in said shell, a conveyor on said shaft for rotation therewith for simultaneously agitating and moving the material through said shell, said conveyor comprising a plurality of helices mounted on said shaft in such relation that helices having a relatively large number oi' turns per inch alternate with helices having a smaller number of turns per inch. the helix closest to the hopper being one having a large number of turns per inch. N

nozzles in said shell adjacent to the helices having a relatively large number of turns per inch for spraying fluid on to the material passing through said shell, and means for tilting said shell from the horizontal whereby the throughput of the material through said shell may be varied without changing the speed of said conveyor, the construction and arrangement being such that the material is moved through the shell by the helices having a large number of turns per inch at a slower rate than by the helices having a smaller number of turns per inch.

MARK PLUNGUIAN.

JESSE L. RILEY.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 363,953 Alexis-Godillot May 31, 1887 644,873 Schweitzer Mar. 6, 1900 992,629 Atkins May 16, 1911 1,002,246 Ellis Sept. 5, 1911 1,498,286 March June 17, 1924 1,702,526 Steely Feb. 19, 1929 2.164.257 Piza June 27. 1939 2,404,884 Pieper July 30, 1946 2,428,789 Dickson Oct. 14, 1947