US1535146A

US1535146A - Method of heating gaseous fluids

Info

Publication number: US1535146A
Application number: US610720A
Authority: US
Inventors: Herman A Brassert; Charles W Andrews
Original assignee: Individual
Current assignee: Individual
Priority date: 1923-01-04
Filing date: 1923-01-04
Publication date: 1925-04-28
Anticipated expiration: 1942-04-28

Description

April 28, 1925.

H A. BRASSERT ET AL METHOD OF HEATING GASEOUS FLUIDS Filed Jan. 4, 1923 Patented Apr. 28, 1925.

PATENT oFFicE.

HERMAN a BRessEnT, or onrcnso', ILLINOIS, AND

DULUTH, mmmsora METHOD or HEATING GASEOUS rnums.

Application filed January 4, 1923. Serial rm. 610,720.

To all whom it may concern:

Be it known that we, HERMAn A. Bass sum and CHARLES W. ANDREWS, citizens of the United States, residing respectively, at

6 Chicago, in. the county of Cook and State of Illinois, and at Duluth, in the county of St. Louis and State of Minnesota, have jointly invented certain new and useful Improvements in Methods of Heating Gaseous Fluids, of which the following is a specification.

This invention, relates to a new and improved method of heating gases and more particularly to a method adapted for use in heating blast air, gases or steam in connection with gas producers, water-gas machines,

blast furnaces, or the like.

Heretofore, gases have been commonly heated for these purposes eitherby continuous recuperation or by regeneration through periodical reversals, the period being relatlvely long, generally one hour in duration. Regeneration with cycles of such length involves heat storage apparatus of sufiicient capacity to store all the heat which is to be given up by the regenerator and absorbed by the gases during the one hour period of heat delivery.

This method has numerous disadvantages 39 in that it involves a large installation of high initial cost, as well as high repair and maintenance charges in connection with the regenerator brickwork. A further disadvantage consists in the great radiation losses through the extensive surfaces of the large heat storage apparatus. Such a method also involves undesirable characteristics in that there is a gradual but substantial drop in the temperature of the gases heated by the 40 apparatus during the one hour heat delivery 5% this combination permitting regeneration 111 short cycles so that there may be nosubstantial drop in the temperature oi? the gases heated by the regenerators. The method thus requires no regulation to afford a uniform temperature curve.

Our invention is best carried out by the use of a plurality of stovesfilled with heat absorbing material, such as fire brick or metal, or a combination of both. The stoves alternately are heated by the combustion of gases and give oi? the accumulated heat to the gaseous medium to be heated. The reversal takesplace at relatively short periods preferably from five to ten minutes, and may be automatically controlled by mechanical or electrical means.

It is an object of the present invention to provide a new and improved method for the heating of gases whichmethod comprises regeneration by means of short heat absorbing and heat discharging periods for each generation unit whereby-a relatively even view showing a three-unit installation;

. Figure 2 1s an elevation of the installation of Figure 1 taken on line 2-2; and

Figure 3 is. a verticalsection of one of the regenerator units.

The installation shown in Figuresl and 2 comprises the three regenerator units A, B and O, and the stack D. These three units are provided with

air inlet passages

8, 9 and 10, respectively, these passages being controlled by

valves

11, 12 and 13. The units are also connected at their upper ends with the gas heater 1% by means of

passages

15, 16 and 17, controlled by

valves

18,19 and 20, respectively. The IDlZfiITQlfi-tlOH of the air and gas passages at their point of entrance into the unit is best shown in Figure As shown in this figure, the air passage 8 encircles the downwardly directed portion 21 of the gas passage 15, and the two passages terminate within the upper portion of the unit A forming a burner.

The upper portions of the units A, B and C are connected to the hot gas header 22 by

passages

23, 24 and 25, controlled by

valves

26, 27 and 28, respectively. The lower portions of the regenerator units are connected to stack D by

passages

29, 30 and 31, controlled by

valves

32, 33 and 34, respectively. The lower portions of the units are also connected to the cold gas header 35 by

passages

36, 37 and 38, controlled by

valves

39, 40 and 41, respectively. The lower ends of the unit are provided with clean-out doors 42, as shown in Figure 3, for the removal of waste material accumulating in the units.

The units in the form shown in Figure 3 comprise an outer metal shell 43 and inner refractory lining 44, the heat absorbing brick checkerwork 45, and the heat absorbing metal rods 46.

In the operation of the installation according to our method, gas is introduced into the tops of the units from header 14 through the

passages

15, 16 and 17, and air is simultaneously introduced through

passages

8, 9 and 10. The gas is introduced under pressure and induces the flow of air through the surrounding passage. The gas is burned in the upper portion of the regenerator units. The

flame impinges upon the brick checkerwork' 45 and the heated products of combustion pass down through metal rods 46 which are aid upon each other in reversed directions and in staggered relation so as to provide passage for the gas. The products of comustion pass out through

passages

29, 30 and 31 to the stack D. It will be understood, of course, that the heat remaining in the gases may be utilized in waste heat boilers or in anyother apparatus.

The gas utilized in heating the regenerators may be any type of combustible gas such as producer gas, water gas or natural gas, or may be blast-furnace or other similar gases. The gas may already have ahigh temperature when introduced into the regeneratqrs and the sensible heat of the gas may play a material part in heating the regenerators.

When a regenerator is sufhcientl heated, its supply of air and gas is cut 0 by closing the necessary valves such as

valves

11 and 18 in connection with unit A. Its communication with the stack is shut 01f by closing valve 32. The air, gas or steam to be heated is now introduced from header 35 through passage 36, valve 39 being 0 en. The fluid to be heated is thus introduce at the lower or cooler portion of the regenerator and passes up through the metal rods and thence through the heated checkerwork, absorbing heat as it rises. The valve 26 is opened and the fiuid passes through passage 23 to the hot header 22 which carries it to thedapparatus in which it is intended to be use The metal rods are particularly efficient in quickly absorbing heat and in quickly giving it off. It is, therefore, possible to pass the gases through the regenerator with considerable velocity and yet to acquire the desired raise in temperature. This portion of the cycle continues for a short period, preferably about five or ten minutes, and in this short period the temperature of the regenerator has not been so lowered as to cause a material change in the temperature of the heated gas passing from the regenerator. At the end of this period, unit A is put on blast, unit B is cut 01? from blast, and the fluid to be heated is introduced into unit B where it is heated as just described in connection with unit A.

By the use of three units, as shown, each unit may be held twice as long upon the heat-absorbing portion of the cycle as upon the heat discharging portion, and adequate temperatures may thus be maintained. It will be understood, of course, that it is possible to carry out our method by using merely two units, one being upon blast while the other is delivering heat. With either two or more units, a continuous flow of substantially uniformly heated gas is assured by our method without the necessity for regulation by means of intermixing cold air or other means of maintaining a uniform temperature curve.

It will be understood that our method can be carried out b other forms of apparatus than that speci cally illustrated and it is our intention to cover such modifications as come within the scope of the appended claims.

We claim:

1. The method of heating gases adapted for heating blast air or steam, which method comprises regeneration by means of short heat absorbing and heat discharging periods for each regeneration unit, the periods being of such duration that a relatively even temperature of the v heated gases may be maintained throughout the heat discharging period without regulation or mixing of gases.

2. The method of heating gases adapted for heating blast air or steam, which method comprises regeneration by means of short cycles of regeneration" using small units adapted to rapidly absorb and give off heat whereby a relatively even temperature of the heated gases may be maintained throughout the heat discharging period without regulation or mixing of gases.

3. The method of heating gases adapted for heating blast air or steam, which method comprises regeneration by means of short cycles of regeneration usin small units adaptedto rapidly absorb an give ofi. heat, a plurahty of units being used whereby each unit may undergo the heat absorbing portion of the cycle for a longer period than it is used to give off heat, and whereby a relatively even temperature of the heated gases may be maintained throughout the heat discharging period without regulation or mixing of gases.

4:- The method of heating gases adapted for heating blast air, or steam, which method comprises regeneration by heatin masses of metal, and thereafter passing t e gases to be heated into contact with said metal for a short period, the periods being of such duration that the temperature of the heated gases is not materially less at the end of the period than at the beginning.

5. ,The method of heating gases adapted for heating blast air,'or steam, which method comprises regeneration by heating masses-of metal, and thereafter passing the gases to be heated into contact with said metal for a short period, the periods being of such duration that the temperature of the heated gases is not materially less at the end of the period than at the beginning, the operation being carried out by means of a plurality of units whereby the masses of metal may be heated for periods longer than their heat delivery periods and whereby a continuous flow of uniformly heated gas may be delivered.

6. The method of heating gases adapted for heating blast air or steam which method comprises regeneration by heating masses of fire brick and metal and thereafter pass ing the gases to'be heated into conta'ct'with said fire brick and metal for a short period, the period being such that the temperature of the. heated gases is not materially less at the end of the period than at the beginning.

7. The method of heating gases adapted for heating blast air or steam which method comprises regeneration by heating masses of fire brick and thereafter passing the gases to be heated into contact with said fire brick for a short period, the period being such that the temperature of the heated gases is not materially less at the end of the period than at the beginning.

Signed at Chicago, Illinois, this-23rd day of December, 1922.

HERMAN A. BRASSERT.

Signed at Duluth, Minnesota, this 18th day of December, 1922.

CHARLES W. ANDREWS.