US1686719A

US1686719A - Fuel-pulverizing system

Info

Publication number: US1686719A
Application number: US199474A
Authority: US
Inventors: Wilfred R Wood
Original assignee: Int Comb Eng Corp
Current assignee: International Combustion Engineering Corp
Priority date: 1927-06-17
Filing date: 1927-06-17
Publication date: 1928-10-09
Anticipated expiration: 1945-10-09
Also published as: FR655672A

Description

0a. 9, 192& 1,686,719

W. R. WOOD FUEL PULVERI Z ING SYSTEM Filed June 17, 1927 ATTORNEYS Patented Oct. 9, 1928.

UNITED STATES 1,686,719 PATENT "OFFICE.

WIIJ'RED R. WOOD, OF LONDON, ENGLAND, ASSIGNOB TO INTERNATIONAL COMBUS- TION ENGINEERING CORPORATION, OF NEW YORK, N. Y., A CORPORATION OF ELAWARE.

FUEL-PULVEBIZING SYSTEM.

Application filed June 17, 1927. Serial No. 199,474.

being abstracted from the system to make the arrangement eflfective.

It has also been proposed to dispense with a dryer by making t e mill function as a dryer, to'which end an appreciable quantity I of adequate hot air or hot gas is introduced into the system through the mill and-a corresponding amount of gas in the system 90 withdrawn therefrom. I

In either. case, difiiculty has been encountered because of the carrying off of pulverized material in the gas so withdrawn, this being especially so when the mill functions as a dryer when the gas in the system is relatively'dry, under which condition the separator, I have discovered, does not func-. tion as effectively as it does withsome of the moisture laden gas.

The primary object of my invention is to enable the gas to be withdrawn 'from the system without this diificulty by simple and effective mechanism. I

How the foregoing together with such other objects and advantages as may hereinafter appear, or are incident to my'invention, are realized is illustrated in preferred form in the accompanying drawings where'- 0 p The figure is a side elevation of a system embodying my invention.

Referring to the drawing, it will be seen that the system comprises, in general, a pulverizer mill A, a separator B, suitable connection 0 between the mill and separator,-

and suitable return connection D etween the separator and mill. 1

Goal to be crushed in the mill A is conducted thereto by means of the pipe 2 which leads from any suitable source of supply of raw coal. A fan 3 is locatedin the connection or conduit C for setting up a gas current through the s stem. In order to prevent the system rom becoming moisture laden, a. portion of the return air or gas is discharged from the system through the pipe 7, and a corresponding quantity of dryer air or gas is introduced into the system through the mill by means of the pipe 4. Similarly, if the mill is to function as a .dryer, sufiiciently hot air or hot gas is introduced into the system by means of the conduit 4 which may be connected, for example, with a furnace flue so as to conduct hot flue gas to the pulverizer mill.

The coal, after being pulverized in the mill, is conductedby the current of gas to the cyclone separator B where the coal and air are,separated. The s arated coal is discharged from the separato at the bottom through the pipe 5 which may-lead to a desired point, as to a storage bin. The circulating gas, together with any coal particles nOtsepara'ted, is returned to the mill by means of the return. connection or conduit D.

In order to reduce the amount of pulverized material carried off from the system with the gas withdrawn as above described, I'have provided means indicated at E in the return connection for withdrawing or exhausting gas in an amount corresponding to the amount of gas introduced into the system. The device E is so constructed as to separate the coal particles from the gas to be discharged, and, in this instance, com prises a drum-like portion 6 in the return line D which is preferably horizontally disposed, and the coaxial gas outlet pipe 7 extending into the drum-like portion and terminating short of an end of the drum as indicated at S. The pipe 9 or the line D lea'ds from-the cyclone separator B to the periphery of' the drum 6 at one end thereof, and discharges its contents tangentially into the drum. The pipe 10 'of the line D'leads from the periphery ofthe drum 6 at the other end thereof to the pulverizer mill A.

The coal particles and gas entering, as they do, tangentially, are swirled about in the drum, which causes the coal particles to be centrifugally separated from the air, and, finally, are discharged into the pipe 10 for return to the mill. Any accumulation of coal particles within the drum "may be led ofi'through the pipe 11 to any desired point, as to a storage bin, to which the pipe 5'may also lead. .Having thus centrifugally separated the coal particles, it will be observed that gas clear of coal enters the open end of the pipe 7 at 8 as indicated by the arrows and exhausts from the system. In fact, I am enabled to separate in the drum E about ninety percent or more of the material in suspension inthe returning gas, which makes it possible to have the pipe 7 discharge into the room if so desired.

From the foregoing it Will be seen that I have provided simple and effective means whereby I can abstract the required amount of gas from the system Without carrying off pulverized material.

Although I have shown the pipe 7 as lead ing from the separator E, it is obvious that it need not be so located. 1

1. In a pulverizing system, a mill, a separator, a pipe between the mill and separator,

a return pipe from the separator to the mill,

means for setting up a current of a' gas through the system, means for exhausting a port on of the gas in the system from the return side thereof, a centrifugal separator in the retu-rnflinc and from which said gas to be exhausted is Withdrawn, means for introducing a relatively dry gas into the system' in an amount corresponding to the amount of gas Withdrawn.

2. 111 2. pulverized system, a mill, a separater, a pipe between the mill and separator, a'ret'urn line from the separator to the mill, means for setting up a current of a gas through the system, said return line including a separator-and means for exhausting a portion of the gas separated thereby from the system, and means for introducing a relatively dry gas into the system in an amount corresponding to the amount of gas exhausted.

3. In a pulverizing system, a mill; a separator; a connection between the mill and separator; a return connection from the separator to the mill; means for settin u a a current of a gas through the system; said return connection including a drum tangentially receiving the gas and fuel particles delivered from said separator into said return line, tangentially delivering gas and.

fuel particles therefrom to the mill, and radially exhausting a portion of the gas from the system; and means for introducing a relatively dry gas into the system in an amount corresponding to the amount of gas exhausted.

4. In a pulverizing system, a mill; a separator; a connection between the mill and separator; a return connection from the separator to the mill; means for setting up a current of gas through the system; said return connection including a horizontally disposed drum-like portion adapted to centrifugally separate fuel particles from the gas being passed through said connection and an axially disposed pipe extending into said drum-like portion and terminating short of an end thereof for discharging a portion of the gas from the system; and

an amount corresponding to that discharged.

5. A fuel pulverizing system including a mill. having an inlet for fuel'to be pulverized, a separator, a delivery conduit between the mill and separator, a return connection between the separator and the mill, means for admitting fluid to the system, a fan in said delivery conduit for setting up a fluid current in the system, said return connection comprising a drum, a pipe leading from the separator to the drum arranged to tangentially discharge its contents into said drum, anda pipe leading from the drum to the mill arranged to tangentially receive its contents from the drum, and means for discharging a predetermined amount of fluid from said drum.

6. The combination in a pulverizing system of the so-called closed type and employing a mill, a separator, a pipe from mill to separator, a return pipe from separator to mill, and means for setting up a current ofwgas through the system, of means for introducing a gas into the system through the mill sufficiently hot to cause the mill to function as a drier as Well as a pulverizer, a second separator in the return line for separating pulverized material from the returning air not separated in the first separator, and an outlet for discharging air from the system separated by said second separator.

In testimony whereof I have hereunto signed my name.

VVILFRED R. WOOD.

means for introducing gas into the system in