US1505057A

US1505057A - Coal-distilling apparatus

Info

Publication number: US1505057A
Application number: US555555A
Authority: US
Inventors: Nagel William Frank
Original assignee: Individual
Current assignee: Individual
Priority date: 1922-04-19
Filing date: 1922-04-19
Publication date: 1924-08-12
Anticipated expiration: 1941-08-12

Description

\N. F. NAGEL COAL DISTFLLLING APPARATUS Filed April 19 1922 WITNESSES ATTORNEYS Patented Aug. 12, 1924.

UNITED STATES.

"WILLIAM ram NAGEL, or ENSLEY, ALABAMA.

COAL-DISTILLING APPARATUS.

Application filed April 18, 1922.. Serial No. 555,555.

To all whom it may concern:

Be it known that I, WILLIAM F. NAGEL, a citizen of the United States, and a resident of Ensley, in the county of Jefferson and State of Alabama, have invented new and useful Improvements in Coal-Distilling A paratus, of which the following is a fu 1, clear, and exact description.-

This invention relates to a process for treating coal to increase its fuel efliciency and to obtain the volatile matter for the manufacture of coal Icy-products.

Experiments have been carried on f0 many years in order to increase the fuel efficiency of coal and to provide a fuel which burns without giving ofi a great volume of smoke. Coke is one of the fuels obtained by the treating of coal which does not give off a great volume of smoke on burning. Further, for the same weight of coke a greater number of calories of heat are obtained than from the burning of the same weight of coal. Processes for treating coalto obtain therefrom fuels having a high heating value per unit weight and which remove the volatile matter 1n a proper condition for the manufacture of coal by-products are of great importance.

The general object of this invention is the provision of a process for treating coal to remove certain volatile matter, this increasing its fuel efficiency per unit of weight.

A further object is the provision of a process for treating coal to provide a high efliciency fuel by the removal of certain volatile matter and saving said volatile matter for the manufacture of coal by-products.

Another object is the provision of a process for treating coal to obtain an efiicient fuel which on burning gives off practically no smoke.

These objects are accomplished by treating the coal with a gas to dissolve or separate the volatile matter therefrom and to carry it into a washing decanter where the volatile matter is removed from the gas.

These and other objects of the invention will be more clearly understood from the following detailed description and accompanying drawings.

Figure 1 is a vertical section across the i apparatus used in the treating of the coal;

Figure 2 is a section along the line 22, Fi re 1.

igure 3 is a vertical section through a feeding apparatus, showing one possible 7 construction Figure is a diagram of a fuel receiver for attaching to the pipe leading from the conta ner shown in Figure 1.

Referring to the above-mentioned drawfeed the coal 14 onto the conveyor, providing a la er of coal 15 of any desired thickness. T e conveyor 11 is preferably formed of spaced slats or bars as shown. The mechanism which controls the feeding of the coal from the hopper 13 may be of a variety of constructionsand it is not proposed to claim it as part of this invention. The feeding mechanism shown and hereinafter described is however preferably employed. .A pipe 17 leads from the container 10 and it is through this pipe that the fuel, prepared by the treating of the coal, is removed.

The-section of the conveyor 11 which carries the layer of coal 15 divides the container 10, forming two chambers 18 and 19. A pipe 20 leads into the upper chamber 18. An exhausting device 21 communicates with the lower chamber 19 and a decanter 22 is associated with the exhausting device 21.

In the operation of this apparatus, coal 14 from the hopper 13 is fed onto the endless conveyor 11 by a feeding mechanism 16. This feeding mechanism 16 includes a casing 23 connected to the lower end of the hopper. In the upper end of the casing 23 is a feed regulator 32 mounted on a common shaft with the worm wheel 30. A worm 31 for operatin the worm wheel 30 is mounted on a shaft 28 b a support 25 and the casin 23. Mounted near the outer end of the shaft 28 is a gear 26, which meshes with a gear 34 fixed near the outer end of a shaft 29 also carried by the support 25 and the casing 23. This shaft 29 projects into the lower end of the casing 23 and has mounted thereon a plurality of blades 33. The

shafts

28 and 29 are operated from a motor 24 through a gear-27 mounted on the motor shaft and the gears 34 and 26. In the operation of this device the coal is conveyed from the hopper 13 into the casin 23 by means of the feed regulator 32.

fter it has been projected into the casing it is fed forward onto the conveyor by means of the blades 33. By controlhn the speed of the motor the rate at which t e coal is fed onto the .conveyor may be controlled.

The thickness of the layer and the pressure on the coal projected onto the conveyor may be controlled by varying the speed of I the'feedin mechanism 16. Rollers 12 which operate e endless conveyor 11 may be driven at any speed by any suitable rime mover. As the coal is moved throug .the container 10 by the conveyor 11 it is treated with heated gases and by the time it reaches the pi e 17 through which it is removed from t e container it has been converted into the desired fuel. The treated fuel passes throu h the pipe 17 into the fuel receiver 35. his receiver 35 is provided with two

valves

36 and 37, one being located at the top and the other at therbottom, providing means for removingl the fuel from the container without great y affecting the gas pressure in the container. Gases used for treating the coal are forced into the container throu h the ipe 20 and ass down from the cham r 18 t rough the ayer of coal 15 into the chamber 19 from which they are exhausted b means of the exhausting mechanism 21. he gases exhausted from the chamber 19 are then conveyed into the decanter 22 where they are washed by any usual method for removing the volatile matter which they have removed from the coal.

Coal in its normal state contains a large amount of volatile matter which when the coal is being burned asses off in the form of smoke, carrying'with it a great amount of the heat generated in the burning of the coal. This smoke that passes off when the coal is being burned carries with it valuable coal b -products, or a great portion of the same 111 which so many by-products may be manufactured. From the above it will be seen that two losses occur when coal is burned in its natural state: first, the heat efliciency of the coal is reduced by the coal b -products which include the hydrocarbons 0% a low boiling point passingofl' in smoke carrying away by convection a certain amount of the heat generated in the burnof the coal. A considerable portion of the coal b products are carried off in the smoke an thus the matter from which so many coal by-products can be made is lost.

In the process described above, the coal in its natural state, or after having been treated, is treated with a gas heated to any desired temperature depending on the final result desired so as to remove the volatile matter. The gas which contains the coal byproducts is then washed by an of the usual methods and the coal b -pr ucts obtained therefrom. The fuel tiius obtained by so treating the coal does not contain the volatile matter which tends to carry away by convection the heat generated in the burnmg and the coal by-products have been saved for manufacturing coal by-products.

I would state in conclusion that while the illustrated example constitutes a practical embodiment of my invention, I do not limit myself strictly to the exact details herein illustrated since manifestly the same can be considerably varied without de arting from the spirit of the invention as efined in the apgended claims.

laims:

1. A device of the class described for treating coal to remove the volatile matter therefrom, comprising a container, an endless foraminated conveyor mounted to rotate in the container, means for feeding the coal onto the conveyor at uniform thickness, means for removing the coal from the container after it has been treated, means for projectmg a under pressure into the container and orcing it through the coal located on the conveyor, means for exhausting the gas from the container, and decanter means for washing the. gas to remove the volatile matter therefrom.

2. In a device for treating coal to remove the volatile matter therefrom, a container having a gas inlet in its top, and a coal outlet at one end, an endless foraminated conveyor'mounted in the container and discharging into the outlet of the container, means or feeding coal onto the conveyor, and an exhaust pipe leading from the container out through one side and above the bottom thereof.

3. In a device for heating coal to remove the volatile matter therefrom, a container having its top and bottom inclined downwardly and upwardly respectively from its center to the ends, said container having a gas "inlet in its top at the center of length,

and a coal outlet at one end, an endless conveyor formed of spaced bars, and mounted in the container, means for feeding coal onto the conveyor, and an exhaust pipe leading from below the up er run of the conveyor out through one s1 eof the container.

WILLIAM FRANK NAGEL.