US2650562A - Method and device for visual observation of dense-phase suspensions - Google Patents

Description

SEPL 1, 1953 F. aoNAR Erm.

METHOD AND DEVICE FOR VISUAL OBSERVATION oF nENsE-PHASE susPENsIoNs Filed nec. e, 1951 lll mvENToRs Floyd Bonar E PVJN D n lu.. A O C Patented Sept. l, 1953 METHOD AND DEVICE FOR VISUAL OBSER- VATION 0F DEN SE -PHASE SUSPENSION S Floyd Bonar and Coultas D. Pears, Morgantown, W. Va., assignors to the Government of the United States as represented by the Secretary of the Interior Application December 6, 1951, Serial No. .260,296 6 Claims. (Cl. 116-117) (Granted under Title 3-5, U. S. Code (1952),

sec. 266) The invention herein described and claimed may be manufactured and used by or for the Government of the United States of America for governmental purposes without payment of royalties thereon or therefor.

This invention is concerned with a method and device for permitting visual observation of a dense phase, solids-in-gas suspension flowing through a conduit.

In the pneumatic conveying of pulverant materials it is often desirable to have some means for visually observing the flow of the material through the conveying conduit. In ordinary methods of pneumatic conveying, where the solids-in-gas suspension is relatively dilute (having a solids:gas volume ratio of the order of 1:100), and where the suspension flows at a relatively high velocity (75 feet per second, for example). it is usually possible to readily observe the flow through the conduit merely by providing a transparent section therein. Even when conveying materials such as pulverized coal, which tend to deposit an opaque lm upon the Walls of the conveying conduit, the turbulence and scrubbing action of a relatively high velocity suspension tends to keep the walls clean and makes visual observation possible through a transparent section of the conduit.

It has been found however, that when employing dense phase suspensions (having a solids:gas volume ratio of the order of 1:4 to 1:8, for example) which move at relatively low velocities (8 feet per second, for example), it is often diilicult to observe the flow of the solid material through a transparent section of the conduit. The low velocity and lack of turbulence in the suspension makes it rather diicult to detect any movement in the suspension even when the Walls of the conduit remain clean. When conveying a material such as pulverized coal, the difficulty is exaggerated since the conduit walls tend to become coated with a film of coal particles.

It is the principal object of the present invention to provide a convenient and reliable method for visually observing a, dense phase solids-ingas suspension as it flows through a conveying conduit. Ancillary objects of the invention will be apparent from the description which follows.

In accordance with the invention it has been found that visual observation of a dense-phase suspension flowing through a conduit may be obtained by providing a relatively small gap in the conduit and continuously flowing an extraneously supplied gas stream through this gap into the 2 conduit at a velocity sufcient to prevent disentrainment or separation of solid material at the gap. With such an arrangement, the dense phase suspension will be clearly visible as an opaque cylinder bridging the gap in the conduit.

To carry out the `foregoing method, the section of the conduit including the gap is enclosed in a gas-tight housing which is provided with at least one transparent wall to permit visual observation of the interior thereof. A gas; stream from an external source is directed into the housing at such a rate that the gas velocity through the gap into the conduit is suicient to prevent the solids from separating from the suspension as it crosses the gap. Preferably, the incoming gas stream is jetted against the transparent wall, or Walls of the housing to prevent the accumulation thereon of relatively small amounts of solids which may become disengaged from the suspension.

For a better understanding of the invention, reference is now made to the accompanying drawings, wherein:

Fig. l is a side elevation of a device constructed in accordance with the invention, together with a semidiagrammatic illustration of an apparatus for supplying a dense-phase solids-in-gas suspension; and,

Fig. 2 is a section taken on line 2-2 of Fig. 1; and,

Fig. 3 is a section taken on line 3 3 of Fig. 1.

Referring now particularly to Fig. 1, the reference numeral I refers generally to a device for supplying an extremely dense phase, solids-ingas suspension to a conveying conduit 2. The device comprises a closed vessel 3 which is charged with a timely-divided solid material, such as pulverized coal, from a hopper 4. A gas stream is introduced into the bottom of the vessel and is passed upwardly through the finely-divided material at a velocity so adjusted that the mass of finely-divided material is converted into the socalled uidized condition. Most of the uidizing gas stream is withdrawn from the top of the vessel through line 6 and may either be vented to the atmosphere, or if desired, recirculated to the bottom of the vessel. A minor portion of the uidizing gas stream ilows out of the vessel through tube 8 as carrier gas for the suspension.

In the so-called fluidized condition, which results when the linear velocity of the gas stream passing upwardly through the mass of nelydivided solid material is within a rather critical range, the individual particles of the mass be- E come suspended, as it were, in the uidizing gas stream, but do not become entrained therein. The mass as a whole resembles a liquid at its boiling point, and as a matter of fact possesses many of the properties of a liquid; it has a deiinite, though turbulent upper surface (indicated by the numeral 'I in the drawing) exerts a pseudo-hydrostatic pressure on the walls and bottom of the vessel in which it is contained; and likewise has many of the flow properties of a liquid.

The range or gas velocities over which fluidization occurs depends chiefly upon the density and size of the individual particles. With coal pulverized to a size through about 100 mesh, iiuidization occurs at superficial linear gas Velocities of from .08 to .3 foot per second, for example. Below this range, the particles in the vessel remain in the settled state; while above this range the particles become entrained in the gas stream and are carried out of the vessel.

One outstanding characteristic of the so-called uidized suspension is that it contains an extremely high concentration of solids. The solidszgas volume ratio, is ordinarily of the order of from 1:4 to 1:8. For a material having a density equivalent to that of coal, such suspensions contain from 98% to 99% by weight of solids.

In order to deliver this extremely dense phase suspension to the conveying conduit 2, an upright tube 8 is provided having an opening within the uidized mass in the vessel 3. The uidized suspension flows into the open end of tube 8 in much the same way as a liquid ows into the open end of a'pipe. The pseudo-hydrostatic pressure exerted by the head of iiuidized material above the opening provides energy for driving the suspension through the conveying conduit 2. Preferably, this driving force is supplemented by maintaining a superatmospheric pressure within the vessel 3 by creating any desired back pressure in the vessel by suitable adjustment of back pressure valve 6a in line 6. A funnel shaped dei-lector 9 is disposed around the open end of the tube 8 to provide a settling zone adjacent the opening. The foregoing method for supplying a densephase suspension to a conveying conduit is described in more detail in copending application Ser. No. 103,502, led July '7, 1949, for Method of Feeding Coal or Other Pulverized Solids .to a Zone of Utilization by Charles W. Albright et al.

In order to permit visual observation of the dense phase suspension owing in conduit 2, a relatively small gap, indicated by the reference numeral I is provided in the conduit. rIhe portion of the conduit including the gap is enclosed in a gas-tight housing II. In the embodiment shown, the housing II is constructed in a manner similar to a pipe cross, each arm of which has an inside diameter substantially larger than the conveying conduit 2. The conveying conduit 2 passes through one arm of the cross, with the gap l0 located at the center of the cross. The other arm of the cross is provided at both ends with transparent or translucent windows.

Referring to Figures 2 and 3, it can be seen that in the embodiment shown, two glass windows l2 and I2a respectively are provided, held in place by internally threaded retaining members I3, which are threaded onto an externally threaded portion of the housing II. Gaskets I4 and spacing ring I4@ provide a gas tight seal.

A gas stream, supplied from an external source, is introduced into the housing II by line I5. As can be seen most clearly in Figure 3, line I5 divides into lines I6 and I1, which in turn supply rgap I0 as indicated by the arrows Ia in the drawings. This serves to prevent the disengagement of any substantial amount of the solids in the suspension as the suspension crosses the gap. It has been found that when no auxiliary gas is introduced into the housing I I, or when the `amount of gas introduced into the housing is insuicient to maintain a certain minimum velocity in the gap, the solids separate from the suspension at the gap at such a rate that the housing quickly becomes lled with disentrained solids, eventually plugging conveying conduit 2. While a small amount of solids may be disengaged at the gap when operating in accordance with the invention, the accumulation of solids in the housing is prevented by the sweeping effect of the gas stream introduced through line I5. Stray particles are re-entrained in this gas stream and carried back into conveying conduit 2.

The minimum gas velocity through the gap I0 which is necessary to prevent substantial disentrainment of the solids at the gap will vary somewhat from system to system depending upon such factors as the size of Ithe gap, the dimensions of conduit, and the particular type of solids-in-gas suspension employed.

In one particular instance, employing a coalin-air suspension at a system pressure of p. s. i. a. and having a solids-to-gas ratio of about 23.1bs. of coal per SCF gas, flowing at a rate of about 10 feet per second through a conveying conduit having an inside diameter of about 0.368", and in which the length of the gap was .045, it was found that it was necessary to supply a gas stream to the housing Il at such a rate that the linear velocity of the gas through the gap was about 1.5 feet per second, in order to prevent substantial disentrainment of the solids at the gap. It is to be understood, of course, that gas velocities through the gap greater than the minimum required may be employed.

While the size of the gap is not particularly critical, it is preferable that it be kept relatively small. In most cases, for conveying conduits having an inside diameter of about .25 to .5 inch, a gap length of from about .045 to .6 inch will generally be found suitable. The larger the gap, of course, the greater amount of extraneous gas must be introduced into the conveying conduit in order to maintain the minimum required gas velocity through the gap. Thus, where it is desired to dilute the suspension flowing through the conduit as little as possible, the minimum gap size should be chosen which will still permit clear visual observation of the suspension as it crosses the gap. In this regard, a gap length as little as .045 inch has been found satisfactory.

It is clear, of course, in the embodiment shown, that direct observation or the suspension as it crosses the gap may be had through the transparent windows I2. By providing a light source 28 (Fig. 3) adjacent to one of the windows to illuminate the interior of the housing, observation, of course, is facilitated. If desired, one of the windows, such as window 2a may be constructed of a translucent material such as frosted glass for example. With this type of arrangement, and with a light source illuminating the conduit from the opposite side of the housing, the shadow o1 the conveying conduit 2 together with the shadow of the suspension crossing the gap iii', is cast upon the translucent window i'c. in this Way, the suspension may be observed without looking directly into the housing.

Ii' desired, an automatic device may be provided for detecting stoppage in the flow oi the suspension, A photoelectric cell, for example, may be positioned at the opposite side of the housing Il from the light source. light from this source would not reach the cell because of the opaque suspension crossing the gap. lf a stoppage occurred, light reaching the photoelectric cell would cause it to become activated and operate a signal of some sort to warn of the stoppage.

The invention has been found to oe particularly useful in providing` a means for visualiy observing the now of dense phase suspensions of finely-divided coal. In one particular application in which the invention has been used, the dense phase coal suspension is fed into a gasification reactor where it is converted by the action of steam and oxygen into a mixture of carbon monoxide and hydrogen. In such an application, it has been found convenient to introduce the necessary oxygen needed in the gasication zone into the housing I l, whence it ilows through the gap l0 into the conveying conduit 2. In this Way, one of the necessary reactants is mixed with the coal before it is introduced into the coal gasification chamber and at the same time the necessary gas is introduced into the housing Il to prevent separation of the coal from the suspension as it crosses the gap.

It is to be understood that the above description, together with the specic examples and embodiments described, is intended merely to illustrate the invention, and that the invention is not to be limited thereto, nor in any way except by the scope of the appended claims.

We claim:

1. A method for visually observing the iiow of a dense phase solids-in-gas suspension through a conduit comprising the steps of causing the dense phase suspension flowing through said con- -duit to jump a relatively small gap in said conduit, owing an extraneously supplied tributary gas stream into said gap at a velocity suflicient to prevent separation of solids from said suspension at said gap, and visually observing the flow of said suspension as it crosses said gap.

2. A method for visually observing the :dow of a dense phase solids-in-gas suspension through a conduit comprising the steps of enclosing a section of the conduit in a gas-tight housing, providing a relatively small gap in said conduit Within said housing, Ilowng a gas stream into Ordinarily,

said housing at a rate suflicient to prevent separation of solids from said suspension at said gap, and visually observing the now of said suspension as it crosses said gap.

3. A method for visually observing the flow of a dense phase solids-in-gas suspension through a conduit comprising the steps of enclosing a section of the conduit in a gas tight housing having at least one transparent Wall to permit visual observation of the interior thereof, providing a relatively small gap in said conduit within said housing, flowing a gas stream into said housing at a rate suflicient to prevent separation of solids from said suspension at said gap, directing the gas stream owing into said housing against said transparent Wall so as to effectively dislodge solid material accumulating thereon, and visually observing the ow of said suspension as it crosses said gap.

4. A device for visually observing the ilow of a dense phase solids-in-gas suspension through a conduit comprising a gas-tight housing sur-- rounding a relatively small gap in said conduit, said housing having at least one transparent Wall to permit visual observation of the interior thereof, and means for admitting a gas stream into said housing so as to prevent solids from accumulating on said transparent Wall.

5. A device for visually observing the flow of a dense phase solids-in-gas suspension through a conduit comprising a gas-tight housing surrounding a relatively small gap in said conduit, said housing having at least one transparent Wall to permit visual observation of the interior thereof, and means for directing a gas stream into said housing against the inner side of said transparent Wall so as to eiectively dislodge solid material accumulating thereon.

6. A device for visually observing the ow of a dense phase solids-in-gas suspension through a conduit comprising a gas-tight housing surrounding a relatively small gap in said conduit, said housing having a pair of light transmitting Walls disposed on opposite sides of said gap, a light source adjacent one of said light transmitting walls for illuminating the interior of said housing, and means for directing a gas stream into said housing against the inner sides of said light-transmitting Walls so as to effectively dislodge solid material accumulating thereon and thereby to permit the observation of said solidsin-gas suspension as it crosses said gap.

FLOYD BONAR. COULTAS D. FEARS.

`662,623 Germany July 18, 1938

Images