Method for treating carbonaceous material

April 5, 1938.

R. S. WALKER 2,113,522

METHOD FOR TREATING CARBONACEOUS MATERIAL·

Original Filed Nov. 8, 1934 5 Sheets-Sheet 1

<img file="US2113522A_D0001.tif" />

April 5, 1938.

R. S. WALKER

2,113,522

METHOD FOR TREATING CARBONACEOUS MATERIAL

Original Filed Nov. 8, 1934 5 Sheets-Sheet 2

<img file="US2113522A_D0002.tif" />

<img file="US2113522A_D0003.tif" />

<img file="US2113522A_D0004.tif" />

April 5, 1938.

R. S. WALKER

2,113,522

METHOD FOR TREATING CARBONACEOUS MATERIAL

Original Filed Nov. 8, 1934 5 Sheets-Sheet 3

<img file="US2113522A_D0005.tif" />

<img file="US2113522A_D0006.tif" />

April 5, 1938.

R. S. WALKER

2,113,522

METHOD FOR TREATING CARBONACEOUS MATERIAL

Original Filed Nov. 8, 1934 5 Sheets-Sheet 4

<img file="US2113522A_D0007.tif" />

April 5, 1938.

<img file="US2113522A_D0008.tif" />

R. s. walker 2,113,522

METHOD FOR TREATING CARBONACEOUS MATERIAL

Original Filed Nov. 8, 1934 5 Sheets-Sheet 5

<img file="US2113522A_D0009.tif" />

Patented Apr. 5, 1938

2,113,522

UNITED STATES PATENT OFFICE

2,113,522

METHOD FOR TREATING CARBONACEOUS MATERIAL

Robert S. Walker, Bellefonte, Pa., assignor to Electro Lime &amp; Ice Corporation, Wilmington, Del., a corporation of Delaware

Application November 8, 1934, Serial No. 752,174

Renewed September 7, 1937 (CI. 263—53) bon dioxide is caused to travel therethrough and impart its heat to the material which liberates more carbon dioxide. This heated carbon dioxide in its circulation is caused to travel through a heating chamber in direct contact with an elec- ₅trical heating medium which is inert to the gas and does not tend to impart impurities thereto. I have discovered that, in this manner, the gas may be raised to a temperature, for example 2000° F., sufficient to reduce or calcinate the stream or streams of carbonaceous material as it travels therethrough. I find it highly desirable to maintain the pressure in the calcining chamber where the gas contacts with the material below atmospheric, at least throughout a substan- 15 tial part of the chamber, and to maintain the chamber closed so that air is excluded. It is essential that a thorough distribution of the gas throughout the streams of carbonaceous material be obtained in order to make full use of the _2Qheat imparted to the gas in the heating chamber. In some parts of the chamber pressure above atmospheric may be produced without materially affecting the efficiency of the process.

The use of an electrical heating medium to ₂₅impart heat indirectly to the material, e. g., through a circulation of gas, has been found preferable in some instances to a direct electrical heating of the material as described in my former applications. 30

I am aware that it has heretofore been proposed in the manufacture of carbonic acid gas by a contact process in which heated gas is circulated through the carbonaceous material, and such a process is disclosed, for example, in the 35 patent to Luhman, No. 706,972, August 12, 1902 and in the patent to Knox, No. 768,230, August 23, 1904. But so far as I am aware, such processes have never been found practicable, for the reason that the gas in its circulation becomes im- 40 pure, for example, by reason of exposure to the products of combustion or contact with air. Moreover, in such processes where the gas is not subjected to direct contact with products of combustion, it has not been found possible to raise 45 the gas to temperatures sufficiently high to calcinate the material. For these and other reasons, such processes have not been employed commer- , cially.

I utilize the essential features of my original 50 process, namely, (a) the use of an electrical heating medium, (b) the travelling of the material in a stream or streams in a closed chamber, (c) an atmosphere inert to the gas, and (d) a subatmospheric pressure in at least a portion of the 55

Claims.

The present invention is an improved method and apparatus for treating carbonaceous material, and is an improvement upon the method and apparatus disclosed in my copending applications, Serial No. 553,583, Method for treating limestone, ⁵ filed July 28, 1931, and Serial No. 691,898, Apparatus for treating limestone, filed October 2, 1933

In my former applications, I have disclosed a method wherein the material is caused to flow or gravitate in a stream, and, at the same time, is directly subjected to heat in an atmosphere inert to the gas, for example, heat produced by an electrical heating medium, in a chamber from which 15 air is excluded and wherein a sub-atmospheric pressure is maintained. This method permits continuous operation in an economical and efficient manner, and the production of substantially pure carbon dioxide. I have discovered that when carbonaceous material is calcined at atmos2⁰ pheric pressure in a carbon dioxide atmosphere, the carbon dioxide tends to cling about the limestone, thereby retarding liberation of further gas and tending to cause re-absorption of the carbon dioxide. I have further discovered that ²⁵ when the treatment is carried on at sub-atmospheric pressure this difficulty is overcome, since the specific gravity of the gas is reduced and it tends to move quickly away from the materials and reduce partial pressure. When the air is ex³⁰ eluded and an inert atmosphere maintained, as can be done with an electrical heating means, it is possible to produce a very pure carbon dioxide in an economical manner. By “inert atmos35 phere”, I mean one that does not affect the purity ° of the carbon dioxide.

The present invention employs these highly valuable features of my process in a somewhat different manner. I have now discovered that it ₄₀ is possible to reduce the carbonaceous material without directly subjecting the same to the electrical heating medium provided the material is caused to gravitate or flow in relatively thin streams, and is thoroughly subjected to a heating ₄5 medium in an inert atmosphere, such as the released heated carbon dioxide which is circulated through streams of material. In other words, if the material, through at least a part of the calcining chamber, is maintained under sub-atmos50 pheric pressure and is subjected to a countercurrent of highly heated carbon dioxide gas free of impurity while air is excluded, the process is more efficient. That is to say, while the material is caused to flow or gravitate in a thin stream or 55 streams, a countercurrent of highly heated car2,113,522 chamber. But I have found it possible to dispense with the direct application of the electrical heat and to apply heat to the material from an electrical heating medium by employing the cir5 culating gas as a heating agent.

An object of the invention is to provide a simple, efficient and economical method and apparatus for treating carbonaceous material, in which a portion of the gas evolved during calci10 nation is withdrawn in pure condition from the calcining chamber, electically heated and returned to the calcining chamber in the same pure condition to constitute heat circulating means for effecting calcination of the material.

Another object of the invention is to provide a new and improved method and apparatus for recovering pure carbon dioxide gas directly from the reduction of limestone into lime.

A further object is to provide a method for 20 thoroughly subjecting the material to the heat in a closed calcining chamber by interrupting and dividing the material into a stream or streams as it passes through the calcining chamber, thereby insuring substantially uniform distribu25 tion of the heat throughout the material and calcining chamber.

A further object comprehends the provision of a calcining apparatus including interrupting or retarding means for separating the material in30 to thin streams, such means comprising spaced rows of horizontally and vertically offset refractory members, each member of the rows being staggered or offset relative to the adjacent upper and lower member, so that the material, as it 3a passes through the calcining chamber, will be continuously and progressively divided into thin streams to insure thorough calcination.

Another object is to insure the uniform distribution of the heated gas as it passes through the 40 chamber, thus preventing the material in certain areas of the chamber being subjected to a degree of heat differing from the heat applied to material in other areas.

A characteristic feature of the apparatus is a 45 closed calcining chamber and a communicating heating chamber, the calcining chamber being provided with means for allowing a portion of the evolved gas as it circulates through the chamber to be confined within the calcining chamber 50 without contacting with the material, and also with means which permits another portion of the heated gas to contact with the material. These two separate portions of the heated gas thus constitute direct and indirect means for in55 surlng the complete calcination of the material as it passes through the calcining chamber. Additionally, the calcining chamber has interrupting means therein for dividing the charge into thin streams that are fed in substantially spiral θθ or sinuous paths through the calcining chamber.

Another feature of the invention consists in associating a soaking pit with the calcining chamber and providing the soaking pit with heating means to insure the thorough calcination of 65 the material before it is discharged from the apparatus and prevent a drop in temperature from radiation losses.

A still further feature of the invention is a construction adapted to provide a battery of fur70 naces for treating carbonaceous material which may be increased or reduced in number as conditions warrant. Each furnace may comprise a calcining chamber which communicates adjacent its opposed ends with a heating chamber so as 75 to provide a circulating passage for withdrawing the evolved gas and conducting it to the heating chamber where it is heated to the desired temperature prior to being returned to the calcining chamber to treat the material therein.

Other objects and advantages of the invention will become apparent from the following description when taken in conjunction with the accompanying claims and drawings.

Referring to the drawings which disclose several preferred embodiments of the invention, ₁₀figure 1 is a vertical sectional view of my apparatus for treating carbonaceous material with parts in side elevation.

Figure 2 is a sectional view taken substantially along the line 2—2 of figure 1.

figure 3 is a sectional view taken substantially along the line 3—3 of figure 1.

figure 4 is a sectional view taken substantially along the line 4—4 of figure 1.

figure 5 is a sectional view taken substantially along the line 5—5 of figure 1.

figure 6 is a sectional view taken substantially along the line 6—β of figure 1.

figure 7 is a sectional view taken substantially along the line 7—7 of figure 1.

Figure 8 is a developed view showing the arrangement of the interrupting members in the material passage.

figure 9 is an enlarged sectional view of the apparatus taken substantially along the line 9—3 of Figure 7.

Figure 10 is a sectional view taken substantially along the line 10— 10 of Figure 9.

figure 11 is a vertical sectional view of a modified form of the apparatus. 35

Figure 12 is a sectional view taken substantially at right angles to figure 11.

Figure 13 is a sectional view taken along the line 13—13 of figure 12.

Figure 14 is a fragmentary view of the inter- 40 rupting means shown in figure 11, and

Figure 15 is a sectional view of a modified form of receiving tank and closure member which may be substituted for the corresponding parts shown in Figure 11.

The methods heretofore employed in treating carbonaceous material to recover the evolved pure gas have not been commercially feasible due to the fact that these methods are either unsatisfactory or so expensive as to render them prohibitive. It has been customary in most of the prior methods to heat the carbonaceous material by direct contact with the products of combustion of coal or gas so that the evolved carbon dioxide gas mixes with the air and products of _6ΰcombustion, thus necessitating the separating of the impure gases from the carbon dioxide gas before the latter can be recovered in pure condition. Moreover, in view of the large quantity of fuel consumed in heating the carbonaceous material ou to the desired temperature to effect calcination, and also because of the expense in constructing a furnace capable of withstanding the high degree of heat to which the material must be subjected, these methods have not been found _e5mercially successful or economical.

The electric heating of carbonaceous material to obtain the evolved gas in pure form has not been given serious consideration because the cost of electric heating has been regarded as too ex- 70 pensive to produce the pure gas on a scale that would be commercially profitable. One serious objection to the electric heating of carbonaceous, material is that for this method to be efficient the charge should be brought into intimate con- '&lt;

2,113,622 tact with the electrical heating means. If the heating means is composed of material that produces a gas which contaminates or dilutes the carbon dioxide gas when mixed therewith, the 5 impure gas has to be removed before the carbon dioxide gas can be recovered in pure form. Another objection to the electric heating method is that due to the high temperature required to calcinate the material, it is difficult to heat the 10 charge uniformly so that portions of the material are either insufficiently burned or overburned.

In order to overcome the defects heretofore found to be inherent in the electric heating of carbonaceous material to recover the evolved gas 15 in substantially pure form, I have provided a new and improved method in which the evolved pure gas is utilized as the medium for transferring the electrically generated heat to the charge during the calcining operation. This is effected by feed20 ing the carbonaceous material in a thin stream or streams through a closed zone heated by the evolved gas liberated from the material. (The air in the heated zone is first removed so that the material is treated under sub-atmospheric or 25 negative pressure.) The pure carbon dioxide gas as it is evolved is circulated through a heated chamber or passage preferably having an electrical heating unit or units therein. Each heating unit is composed of a suitable resistance 30 which is inert with respect to the evolved carbon dioxide gas so as not to have any deleterious effect on the evolved gas as the latter is brought into intimate contact with the heating unit. In other words, when the carbon dioxide gas contacts with 35 the heating unit no harmful chemical reaction will take place and there will be no formation of a gaseous mixture which would require the separation of the carbon dioxide gas therefrom before the latter can be removed in pure condition. As I the evolved gas passes through the heated chamber or passage its temperature is raised by the heating unit and the heated gas is returned to the heating zone. The pure heated gas then passes through the heated zone in a direction counter to the flow of the stream or streams of the carbonaceous material and at a sufficiently high temperature to produce rapid calcination of the material as the latter is brought into intimate contact with the heated gas.

It will, therefore, be seen that by reason of my improved method, the evolved pure gas is efficiently and economically recovered and may be utilized at sub-atmospheric pressure as the means for transferring heat to the carbonaceous mate_M rial without in any way affecting its purity or requiring further treatment before it is removed from the closed heated zone.

It will be understood, therefore, that the method has certain definite preferred character60 istics, which may be briefly summarized as follows:

(a) The maintenance of a condition within the calcining chamber which will overcome the tendency of the gas to cling to the material, which 05 tendency exists at normal or atmospheric pressure. I prefer a sub-atmospheric pressure throughout a substantial portion of the chamber, although in some instances a pressure substantially higher than atmospheric has been 70 found to accomplish the desired results, provided some, medium which will reduce the partial pressure is admitted into the chamber. Air is objectionable, because of the difficulty in separating the same from the carbon-dioxide, but, as is well known, other media not open to this objection are available and may be used. As has been explained, there is a tendency under atmospheric or super-atmospheric pressure for the liberated carbon dioxide to adhere to or cling about the stone. The maintenance of a condi- 5 tion which will counteract this tendency, is, therefore, highly desirable. The sub-atmospheric pressure tends to stretch or rarefy the gas and in this way contributes to overcoming the tendency of the gas to cling about the stone. Hie 10 degree of vacuum maintained may be materially reduced if the process is carried out by using other media which assists in carrying the gas from the stone, but, in such cases, the media employed must be of a character which will be 15 readily separable from the gas and substantially non-miscible therewith. In certain chemical processes where a mixture of air with carbon dioxide is not objectionable, it may be used, and, in such instances, the pressure may be raised or 20 the degree of vacuum reduced.

(b) Causing the material to flow in a relatively thin stream or streams while continuously subjecting the same to a countercurrent of highly heated pure gas. 25 (c) An electrical heating medium inert to the gas is used to apply heat, preferably in an indirect manner, by recirculating the gas and causing it to pass in direct contact with the electrical heating medium. 30

These essential characteristics of the method enable the same to be practiced in a continuous manner and permit the production of pure carbon dioxide.

A suitable apparatus for practicing my method 35 comprises a unitary kiln or shaft furnace built up or constructed so as to include an outer wall 17 of suitable heat resisting material, such as silocel or red brick, and an inner brick wall or lining It of refractory material which has a high thermal 40 conductivity, such as Are brick or the like. Hie apparatus is enclosed within a steel casing or jacket 19 and may be supported in any suitable manner, as by the frame or uprights 2t.

The intermediate portion of the apparatus con- 45 stitutes a calcining or reducing chamber 21 (Fig. 1) which communicates at its upper end with a material receiving compartment or tank 22 through a reduced portion 23. The charge is delivered to the compartment 22 through a sup- ₆₍j ply pipe or spout 24 controlled by the valve 25. The top of the compartment 22 is closed by a hood or cover 26 which communicates with the supply pipe 24. The lower end of the calcining chamber communicates with a soaking pit 27 which in 55 turn discharges into a tank 25 through the spaced passages or pipes 29. The calcining chamber 21, compartment 22, and soaking pit 27 constitute a vertical passage through which the material passes in a plurality of streams, and these parts eo are enclosed within the refractory wall 18 which in turn is insulated against loss of heat by the insulated wall 17. The apparatus may be of any desired size and shape and when of a twenty-five ton capacity, it has been found that desirable re- 55 suits are obtained by having the internal diameter of the calcining chamber 21 approximately eight feet with a material receiving area of approximately fifty square feet.

Extending upwardly within the soaking pit 27 70 and spaced from the lining 18 is a column 27' of refractory material (Fig. 1). Above the column 27' and in substantially vertical alignment therewith is a tubular or hollow member 30 having therein an axially disposed post or pier 31 which 75

2,113,622 preferably extends the length of the calcining chamber 2 f within the tubular member 30. The space between the tubular member 30 and the post 31 constitutes an annular heating chamber 5 32 which is closed at the upper end of the calcining chamber as by a cap 32'.

The tubular member 30 is also spaced from the inner wall of the calcining chamber 21 to form a passage 33 through which the charge 34 from 10 the compartment or tank 22 passes to be calcinated by the heated gas which passes upwardly through the same passing in a direction counter to the flow of the material.

To insure the thorough calcination of the ma16 terial as it gravitates through the passage 33, means is provided for progressively interrupting and retarding the flow of the charge and dividing the same into thin streams. This means comprises spaced refractory members or blocks 20 35 that are built into the apparatus and extend radially from the tubular member 30 to the inner wall 18 of the calcining chamber (Fig. 4). As illustrated in the developed view shown in Figure 8, the members 35 are arranged in uniformly 25 spaced stepped relation in four spiral rows 36, 37, 38 and 39, each brick being vertically offset, staggered or stepped relative to the adjacent upper brick so as to be in the path of the material as it falls from the upper brick. By reason 30 of this arrangement the material is progressively interrupted and subdivided into thin streams throughout its passage through the calcining chamber. Additionally, the interrupting members serve to distribute the heat uniformly 35 throughout the calcining chamber to insure thorough and complete calcination of the charge.

Within the apparatus, and preferably positioned to one side of the calcining chamber 21, is a heating chamber or passage 43 arranged to 40 be heated by suitable means which will be subsequently described. The heating chamber 43 is preferably formed in a lateral offset portion 44 of. the inner wall 18 and is spaced from the calcining chamber 2i by the refractory wall 44' 45 through which heat may be conducted to the chamber 2 i. The outer wall 17 has an offset portion Π' which encloses the portion 44 and the chamber 43 in the manner as shown in Fig. 4.

At the upper end of the chamber is a gas reser60 voir or collector 45 having a port 46 which communicates with the upper portion of the heated chamber 43 through a pipe 41 in which is positioned a suction fan 4S operated by a motor 49. The reservoir 45 is connected to the inner wall 55 of the calcining chamber by the radially disposed webs or bricks u8 (Pig. 2) which are suitably spaced to allow the charge to fall freely from the compartment 22 to the calcining chamber 21. In order that a portion of the evolved gas in the 60 calcining chamber 21 may be circulated through the apparatus to heat the material, the passage 33 is arranged to communicate with the reservoir 45 in any suitable manner, and as. shown in Figure 3, this may be effected by positioning be65 neath the webs 50 blocks 51 separated by the spacer blocks 52 so as to form a series of vertical passages 53 and horizontal passages 54 which establish communication between the chamber 33 and reservoir 45 adjacent; the upper end of 70 the tubular member 39 (Fig. 1).

The lower portion of the heating chamber 43 has a laterally disposed port 55 (Fig. 6) which communicates with an annular chamber or passage 56, which in turn communicates with four 76 radial passages 51. The passages 57 lead to the interior of tubular member 30 to conduct a portion of the heated gas from the lower end of the chamber 43 into the tubular member where it is confined due to the fact that the upper end of the member is closed. The heat of the gas 5 is imparted to the material in chamber 21 through the wall of the tubular member. The remaining portion of the heated gas traveling through port 55 is delivered to the lower end of the calcining chamber 21 through the radial 10 ports 58 (Fig. 5) in the wall 59 which separates the passage 56 from the calcining chamber.

It will be seen that the heated gas as it issues from the chamber 43 through the port 55 is divided into two streams, one of which is con- 15 ducted by the ports 57 to the interior of tubular member 30 which is closed at its upper end. The lower end of the chamber 32 communicates with the chamber 33 through the ports Gl formed in the tubular member. The remaining portion 20 of the heated gas passes from the chamber 56 through the openings 58 (Fig. 5) into the calcining chamber and passes upwardly through the material at a sufficiently high temperature to effect rapid calcination. A portion of the gas in 25 the passage 33 is delivered to the reservoir 45 through the passages 53 and 54 where it is drawn by the suction of the fan 48 through the pipe 46 and forced through the.heating chamber 43. The remaining portion of the evolved gas passes up- 30 wardly through the charge 34 to preheat the same, and is withdrawn from the tank 22 through . a pipe 62 by a fan 63 operated by the motor 64.

From the pipe 62 the gas is conducted by a pipe 65 to a storage or receiving tank 66. The con- 35 fined gas in the annular opening or closed passage 32 is allowed to escape slowly through the ports 61 to the passage 33 due to the suction created in the calcining chamber by the fans 48 and 63, so that a constant flow of heated gas 40 from the chamber 43 is delivered to the interior of the tubular member 30 to maintain the same at a uniform temperature.

While any suitable electrical heating means may be employed for heating the circulating gas 45 as it passes through the chamber 43, I prefer to use an electrical heating unit that will be inert to the circulating gas brought into contact therewith; a heating or resistance unit of nichrome metal will serve this purpose. These units 50 may be composed of a series of vertically disposed electric resistance members 67, each of which consists of a grid 67' extending transversely of the chamber 43 (Fig. 5). Leads 68 connect each of the grids 67' to any suitable source of cur- 55 rent or control apparatus so that the temperature in the heating chamber may be varied to heat the material. The grids 67' are separated from the calcining chamber by the wall 44' which serves to protect the heating units 67 and which 60 also prevents the material from passing into the upper portion of the heating chamber 43. The resistance units 67 are capable of producing a temperature of 2000° F. in the chamber 43 which is sufficient to disassociate completely the gas 65 from the material during the calcination operation. Preferably one of the side walls 68 of the chamber 43 is removable so that the heating units 67 may be readily inserted or withdrawn from the heating chamber. In order to facilitate 70 this movement, the inner, wall of the chamber 43 is formed with spaced vertically disposed ledges 69 for slidably receiving each of the heating units G7.

Dust or other foreign matter that may ac- 75

3,113, cumulate within the chamber 43 during the operation of the apparatus may be withdrawn, through the discharge pipes 70 which lead from the lower end of the heating chamber 43 to a dust collector or the like (not shown).

The base of the column 27' extends upwardly in the soaking pit 27 and is provided with a reduced portion 71 to increase the area of the soaking pit. Extending outwardly from the reduced 10 portion 71 are a series of stepped portions 72 that act to increase the heating surface of. the column and assist in calcinating the material in the soaking pit. Means is provided for heating the material in the soaking pit; this may be 15 effected by enclosing the upper end portions of each of the discharge pipes or passages 29 (Fig. 9) within a thin refractory wall 73 which may be heated in any suitable fashion, as by the electrical resistance coils 78 embedded in the wall 73. 20 The maintenance of the material in heated condition in the soaking pit prevents re-absorption of the gas.

In order to insure the withdrawal of the treated material or lime from the apparatus at predeter25 mined intervals so that each charge will be uniformly treated, each of the pipes 29 is provided with a rotatable feeder 74 having spaced blades 75 of substantially the same width as the interior of. the pipe. The feeders 74 are positioned be30 neath elongated openings 76 in the plates 77 to receive the treated charge or lime and conduct it to the tank 28. A drive shaft 79 connected to a motor, not shown, is keyed or otherwise secured to each of the feeders 74 to discharge the material 35 in the pipes 29 to the tank 28 at predetermined intervals during the operation of the apparatus. Each of the blades 75 is associated with the opening 76 so that when the blades are rotated to withdraw the material from the pipes 29, each 40 succeeding blade will be moved to a position medially of the opening 76 (Fig. 10) and will coact with the blade which is being moved away from the opening to prevent any material from escaping between the ends of these blades and the adjacent wall of the pipe.

In operation, the carbonaceous material to be treated, such as limestone, is introduced into the receiving compartment 22 through the spout 24, controlled by the valve 25, and is fed downwardly , through the reduced portion 23 into the calcining chamber 2 i. As the charge passes the spaced webs 50 it is separated and impinges on the upper horizontal row of blocks 36 from where the separate streams successively fall on the lower ad55 jacent offset blocks so as to be continuously subdivided into thin, streams, thus insuring the particles being brought into intimate contact with the heated gas passing upwardly through the apparatus. The relative location of the inter60 rupting members 35 causes the material to pass through the calcining chamber in tortuous or spiral paths, as indicated by the arrows in Fig. 1. The heat confined within the passage 32 serves to heat the tubular member 30 which, in turn, 65 heats the material in the passage 33. During this operation, a portion of the evolved gas is drawn by the suction of the fan 48 through the openings 53 and 54 into the reservoir 45 where its temperature is reduced to about 1200° F. due 70 to the fact that it has given up some of its heat in treating the material in the calcining chamber. This gas is then conducted by the pipes 46 and 47 into the heating chamber 43 where it contacts with the heating units 67 so that its temperature 75 is raised to approximately 2000° F. This heated

533 S gas is then forced through the port 55 where it is divided so that a portion thereof is carried by the passages 57 to the annular opening 32 while the remainder of the heated gas is delivered through the ports 58 into the passage 33 5 and as it passes upwardly, due to the suction created by the fans 48 and 63, it is brought into intimate contact with the thin streams of material to thoroughly heat the same.

As the tubular member is closed at its upper 10 end, the heated gas confined therein will tend to maintain the tubular member 30 sufficiently heated so that this radiant heat will combine with the heat directly applied by the gas in the calcining chamber 21 to insure thorough cal- 15 ci nation of the material. A portion of the evolved pure gas in the chamber 33 is delivered as previously described through the openings 53 and 54 to the reservoir 45 so as to be conducted, to the heating chamber 43 and utilized as the me- 20 dium for transferring the heat to the calcining chamber. The remaining portion of the pure gas in the passage 33 is drawn up by the fan 63 through the compartment 22 to preheat the charge therein and then is conducted by the 25 pipes 62 and 65 to the storage tank 66.

' In the initial operation of the apparatus, the compartment 22 is filled with calcium carbonate or the like, and the valve 25 is cut off so as to completely close the apparatus and the air is 30 withdrawn by the suction of the fan 63. The amount of time required and the duration the material is exposed to the heat varies with the character of the material being treated. When Bellefonte limestone, known as Trenton Ledge, 35 is being treated, and it is desirable to liberate the evolved carbon dioxide gas in substantially pure form, the electrical heating units 67 in the heating chamber 43 will produce a temperature of approximately 2000° F., which is sufficient to 40 effect complete calcination of the material, especially under sub-atmospheric pressure. The evolved gas drawn into the reservoir 45 gives up a portion of its heat by reason of its contact with the raw material or limestone, and is dis- 45 charged into the heating chamber 43 through the -pipes 46 and 47 at a temperature below 1200° F. and 1400° F. As the gas circulates downwardly through the heating chamber 43 and past the heating units 67, its temperature is raised to 50 approximately 2000° F., and at this temperature it is introduced into the calcining chamber in the manner as previously described. As the heating units 67 are formed of suitable material inert to the gas, they have no deleterious effect on the 55 evolved pure gas passing through the passage 43 and allow the heated gas to be returned to the calcining chamber in its pure form.

The exhaustion of the air from the apparatus is ascertained by testing the carbon dioxide pass- 60 ing through the pipe 65 and after the air has been completely withdrawn, the carbon dioxide gas in substantially pure form is delivered to the tank 66 and constitutes a very valuable by-product to be used in the manufacture of solid carbon 65 dioxide more commonly known as “dry ice” in making chalk and for other suitable purposes. When starting the apparatus the fan 63 is preferably operated before the fan 48, to insure the air being withdrawn prior to the circulating of 70 the evolved gas through the calcining and heating chamber.

By maintaining the apparatus constantly at a slight vacuum or under sub-atmospheric pressure, the gas evolved during calcination is im- 75

2,113,522 mediately withdrawn so as to avoid re-carbonization and is allowed to either circulate through the heating chamber 43 and be returned to the calcining chamber to thoroughly heat the ma5 terial therein or is withdrawn from the calcining chamber to preheat the charge in the tank 22 prior to it being delivered to the storage tank 66 by the fan 63. The discharge feeders 14 in the passages 29 are timed to operate at the proper 10 speed to withdraw the lime or treated material from the apparatus as fast as complete calcination takes place.

The method of treating the carbonaceous material is continuous and one charge of the ma15 terial in the tank 22 may be Operated for twentyfour hours without re-charging the same or the discharging of the treated material from the tank 28. When discharged at the end of the treated period, the fan 63 is cut off. Immediate20 ly a carbon dioxide pressure is generated within the apparatus brought about by continued calcination pf the material. As soon as this pressure is disclosed at the gauges 79 and 80, the tank 22 is re-charged and the tank 28 is emptied. 25 The carbon dioxide pressure within the apparatus prevents air from entering the system. This entire operation requires between five to ten minutes. Therefore, very little time is lost due to re-charging the apparatus and discharging the 30 lime or treated material therefrom.

It has been found that when limestone is calcined at atmospheric pressure in a carbon dioxide atmosphere, the evolved carbon dioxide gas has a tendency to cling about the limestone 35 and its natural pressure, due to its weight, not only retards liberation of further gas, but the lime is at such a temperature that it will absorb the carbon dioxide and re-carbonate. It will therefore be seen that by initially withdrawing 40 the air from the apparatus and treating the material at a negative or sub-atmospheric pressure through at least a part of the calcining chamber, these difficulties are eliminated, since the evolved gas is allowed to escape immediately.

in the modified form of the invention shown in Figs. 11 and 12, the apparatus is preferably formed so that sections may be added to or removed from the apparatus in order that batches of material of varying quality or size may be si50 multaneously and separately treated at the same temperature or at different temperatures, as conditions may warrant. The apparatus comprises a shaft furnace 8f having an insulated outer wall 82 and a refractory inner wall or lining 83. The 55 outer wall is enclosed within a steel jacket 84 and may be supported on the ground or on a suitable base by a frame 85.

For the purpose of illustrating the arrangement of the shaft furnaces constituting the ap60 paratus, I have shown three of such furnaces 8i, 87 and 88. It will be understood, of course, that any number of these furnaces may be employed so as to form a battery of devices for simultaneously treating the material in separate 65 batches. As each furnace is identical in construction and operation, only one will be described.

The material to be treated is delivered by the spout 89 to the receiving compartment or tank 70 SO which, as shown, is of elongated shape and is closed by a hood or cover 9i. The calcining or reducing chamber 92 is positioned beneath the tank 90 and has spaced interrupting members or blocks 93 of suitable refractory material , which extend transversely across the inner wall of the calcining chamber to interrupt the flow of the material as it falls therethrough. These blocks are uniformly spaced in longitudinally and vertically disposed rows, the blocks of each horizontal row being offset relative to its ad- 5 jacent upper and lower brick so as to continuously interrupt and divide the material into thin streams as it passes through the calcining chamber 92. A soaking pit 94 receives the treated material as it issues from the calcining chamber. 10 The flow of the material to the soaking pit may be controlled by a slidable gate valve 95 having spaced openings 96 arranged to be moved from beneath the grids or blocks 97 to register with the openings 98 between the grids 97 to permit the 15 material to flow freely into the soaking pit 94. Suitable operating means, either automatic or manual, is provided to actuate the valve; for example, a manually operable handle 99 pivoted to the apparatus as at 100, is connected to the 20 outer end of the valve as at iOl to move the openings 96 into and out of registration with the complementary openings 98 in the bottom of the calcining chamber. The furnace 81 is spaced from the adjacent furnace 87 by a refractory 25 wall 102 and the furnace 87 is spaced from the furnace 88 by a similarly formed wall 103. Each of these walls extends the length and width of the apparatus so as to constitute one side of the receiving compartment 90, the calcining chamber 30 92 and the soaking pit 94. The wall 102 adjacent the calcining chamber has a heating passage 104 in which are positioned electric heating units 105. Each of these units consists of a resistance grid 106 (Fig. 13) connected by the 33 leads 107 to any suitable source of current or control apparatus so as to vary the temperature in the heating chamber. One of the end walls, such as 108, has a removable portion or block 109 to permit the ready removal or insertion of 40 the units 105 into the heating chamber 104.

Formed in each of the walls 102 and 103 adjacent the upper horizontal row H 0 of the interrupting members 93 are a pair of spaced passages or conduits III and 112 (Fig. 12). The 45 passage 111 communicates with the calcining chamber 92 through a series of inclined ports 113 that extend from beneath each of the interrupting members of the upper horizontal row 110. A suction fan 117 operated by a motor 118 50 communicates through the pipe 119 with the passage Hi and through the pipe 120 with the passage 112 so that upon the operation of the fan, a portion of the evolved gas in the calcining chamber 92 is drawn through each of the 55 passages 113 to the passage HI and is carried by the pipe 119 through the fan and discharged by the pipe 120 into the passage 112. From the passage 112 the gas is forced downwardly into the heating chamber 104 through the passage 60 114 so as to be brought into intimate contact with the heating units 105. The heated gas is withdrawn from the bottom of the chamber 104, through the ports 115 and delivered into the lower portion of the calcining chamber 92, at a suf- 65 ficiently high temperature, e. g. 2000° F., to produce rapid calcination of the material, as the latter gravitates downwardly and sub-divided into thin streams by the interrupting members 93. 70

The remaining portion of the evolved gas liberated in the calcining chamber 92 is drawn upwardly through the charge in the receiving compartment 90 by the suction of the fan 121 which communicates with the receiving compartment 75

2,113,522 the pipe 137 to a storage tank, in the manner previously described, may be utilized to pre-heat the charge in the hopper 134 prior to the latter’s introduction into the receiving compartment 90. The material to be treated is initially introduced 5 into the hopper 134 through a spout 138 and after the treated material has been withdrawn from the apparatus, the pre-heated material in the hopper 134 is delivered to the receiving compartment 90 through a spout 139, which is con- 10 trolled by a slidable gate valve 140. The operation of the device is otherwise substantially similar to the apparatus shown in Fig. 11. By reason of this arrangement, the evolved gas is utilized to heat and initiate calcination of the 15 material in the hopper 134 as the heated gas is drawn through the passage 136 on its way to the storage tank through the pipe 137, thereby reducing the time and expense involved in calcinating the charge. ²⁰

It will be observed that in all the forms of the Invention disclosed, the evolved gas liberated during calcination, is utilized as the medium for transmitting the heat to the material, and that very little, if any of this heat is dissipated. More- 25 over, the means provided for continuously and progressively interrupting and retarding the flow of the material and which divides the charge into streams as it gravitates through the calcining nhumber, insures the particles of material being 30 brought into intimate contact with the heated circulated gas so as to effect rapid and thorough calcination of the charge at a minimum of current consumption.

It will be understood that the method and 35 forms of the invention shown for recovering the gas in pure condition from carbonaceous material are merely illustrative of preferred embodiments, and that such changes may be made as fall within the purview of one skilled in the art 40 without departing from the spirit of the invention and the scope of the appended claims.