US2626786A - Automatic consistency control means - Google Patents

Automatic consistency control means Download PDF

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US2626786A
US2626786A US745893A US74589347A US2626786A US 2626786 A US2626786 A US 2626786A US 745893 A US745893 A US 745893A US 74589347 A US74589347 A US 74589347A US 2626786 A US2626786 A US 2626786A
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stock
tank
receptacle
consistency
blades
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Leonard D Mcglothlin
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00Wet end of machines for making continuous webs of paper
    • D21F1/08Regulating consistency
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/82Forming a predetermined ratio of the substances to be mixed by adding a material to be mixed to a mixture in response to a detected feature, e.g. density, radioactivity, consumed power or colour
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/2496Self-proportioning or correlating systems
    • Y10T137/2499Mixture condition maintaining or sensing
    • Y10T137/2506By viscosity or consistency

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  • This invention relates in general to means employed for regulating the consistency of a fluid suspension by automatically controlling the addition of liquid to the suspension.
  • this invention relates to the regulation and control of the consistency of pulp stock, such as that used in the manufacture of paper, especially to stock which has been subjected to cooking in a digester, as, for example, krait paper stock.
  • the stock After the cooking in the digester the stock is delivered or blown into a tank, commonly referred to as a blow tank, from whence the stock is pumped to the washers in order that the liquor in which the stock has been cooked may be separated from the pulp.
  • a tank commonly referred to as a blow tank
  • the stock coming from the digester generally has a consistency of about 15%. It is customary to add enough weak liquor to the stock at this stage to reduce the consistency to about 7%, or 6%, so that the stock can be properly handled by the pumps and delivered to the washers. However, as is well known, it is also essential to control the consistency of the stock so that it will be of fairly uniform consistency when delivered to the washers.
  • An object of the present invention is to provide an improved device for reducing the consistency of the stock, as desired, before the stock is delivered to the washers.
  • Another object of this invention is to provide an improved control means which will operate automatically and efliciently to maintain a uni-' form predetermined consistency in the stock preparatory to its being pumped to the washers.
  • a further object is to provide an automatic consistency control means which will be highly sensitive to changes in the consistency of the stock and thus able to maintain a more accurate control of the consistency.
  • An additional object is to provide a consistency control for stock in which black liquor is utilized but in which no excessive foaming of the black liquor will be developed by the control means employed.
  • Fig. 1 is a sectional elevation of the main portion of my device with the associated elements of the entire control means indicated more or less diagrammatically;
  • Fig. 2 is a plan section taken on line 22 of Fig. 1;
  • Fig. 3 is a fragmentary view, in perspective
  • FIG. 1 and 2 showing a portion of the upper rotating paddle and upper baffle in the tank and the outlet from the tank;
  • Fig. 4 is a transverse vertical section through one of the bafiies corresponding to line 4-4 of Fig. 2.
  • the device includes a main consistency control tank l0, which is preferably cylindrical in shape as indicated.
  • the stock from the digester after being delivered to the usual blow tank, which is indicated at H in Fig. 1, passes through pipeline l2 into the bottom of the consistency control tank II].
  • a suitable valve 13 such as a gate valve, is provided in pipeline (2 to control the rate of flow of the stock into tank In or to shut off the flow entirely when desired.
  • the tank I0 is closed at the top and a stock outlet pipe I4 is connected near the top of tank [0 through which the stock is drawn by pumping means (not shown), and caused to pass to the Washers previously referred to.
  • a clean-out I5 is provided in the bottom of tank l0.
  • These branch inlet pipes connect with the tank III at difierent levels and each inlet pipe is controlled by a separate hand valve 20.
  • the incoming diluting liquor can be distributed in equal amounts simultaneously at different levels, as desired, or the comparative rate of distribution at diiferent levels in the tank can be modified.
  • a supplementary inlet port for the liquor is provided at the entrance end of the pipeline I2 between the valve I3 and the tank, this inlet port being shown at 2I in Fig. 1.
  • a branch pipeline (not shown) for the black liquor is connected to this inlet and is also controlled by a suitable hand valve so that the black liquor can be delivered into the bottom of tank In as well as at the other levels, should this ,be desired.
  • Black liquor delivered into the bottom of tank -IU,'when the stock inlet valve I3 is closed, can also be used for flushing out the bottom of the tank I3.
  • a plurality of baflles 22 extend horizontally within the tank I0. These battles are arranged in pairs at different horizontal levels, as shown in Fig. 1, and the corresponding 'baflies of each pair are arranged in vertical alinement. Thus, as apparent from Fig. 2, these bafiles form two vertical rows. However, these two vertical rows are preferably not diametrically opposite each other. While the baflies extend in horizontal direction, the upper faces of the baffles are inclined so as to form dihedral angles with the horizontal planes in which the lower edges of the baffles lie.
  • the inner end of each baffle 22 is supported by a horizontal brace 23 arranged as shown in Figs. 2, 3 and 4, the inner ends of the braces 23 being connected to the under side of thebailles respectively and the outer ends of the braces being secured to the tank wall a short distance behind the points where the outer. ends of the baflles are secured to the wall.
  • the bottom end of the shaft 24 is rotatably supported in a suitable bearing 25 located in the bottom of the tank.
  • the shaft .24 extends through a packing box 26 placed on the top of tank I0, and this packing box contains packing gland elements and permits convenient access to the packing gland elements.
  • a gear 21 is secured to the top of the shaft and a suitable thrust bearing is provided between the gear 21 and the top of the packing box 26.
  • the horizontal shaft 29 is rotatably mounted in a pair of supporting standards 30 which in turn are supported on channel beams extending over the 'top of the tank II].
  • is keyed to the end of the shaft 29' and is driven from a motor 32 through the intermediaryof a reducing unit '33 and sprocket chain connection.
  • paddle blades 34 are mounted. These paddle blades are secured to brackets which in turn are rigidly mounted in place on the shaft 24.
  • the paddle blades are arranged in pairs, the forward faces of each pair of blades being substantially diametrically opposite each other as shown in Fig. 2. All the blades are of the same size and shape, each blade preferably having a front face constituting a vertical plane surface and a horizontal reinforcing rib on the rear face. The blades are all arranged so that their front faces will face 'in the direction ofrotation of the entire assembly, thus clock-wise as viewed in Fig. 2.
  • the-respective blades 34 of the pairs are not in vertical alinement but are in staggered vertical sequence.
  • Each pair of blades 34 is placed a short distance below a pair of bafiles 22, as shown in Fig. 1.
  • the upper faces of the baffles 22 are 50 arranged thatthey will engage the stock when rotary motion-isi-mparted to it in one direction by the blades 34 (thus when the stock is rotated clock-wise as viewed in Fig. 2).
  • the entire arrangement of paddles and bafiles is such that as each pair of paddles encounters the stock the paddles will produce a mixing and rotary motion and as the rotating stock encounters each pair of baffles the stock will receive an upward thrust.
  • thermocouple watt meter diagrammatically indicated at 35 in Fig. l, which serves to convert wattage to milli-voltage, and which in turn actuates an automatically balancing potentiometer or similar controller, dia grammatically illustrated at 36 in Fig. 1, and this in turn operates a pilot air valve (not shown) controlling the passage of compressed air through the compressed air line 31 to a diaphragm-operated control valve 38 in the pipeline I5.
  • the thermocouple 35, balancing potentiometer and pilot valve 36, and diaphragm valve 38 are all well known and of standard construction and need not be further described.
  • thermocouple 35 and the balancing potentiometer 36, together with the diaphragm valve 38, are so arranged that any load on the motor 32 which exceeds a given minimum will cause the thermocouple watt meter, acting upon the balancing potentiometer which operates the pilot valve in the compressed air line, to permit compressed air to pass to one side of the diaphragm in the diaphragm control valve 38 so as to open the valve 38 against the force of the spring, which spring normally holds the valve closed.
  • This opening of valve 38 permits liquor to pass into the tank I!) through the inlet branch pipes I'I, I8 and I9, as previously mentioned.
  • a receptacle for a fluid suspension for a fluid suspension, an element rotated on a substantially vertical axis in said receptacle, means for delivering a diluting liquid to said receptacle, means for delivering the fluid suspension into the lower portion of said receptacle, means for withdrawing the fluid suspension from the upper portion of said receptacle, a series of paddle blades secured to said rotated element and spaced at different heights on said element, the forward faces of said blades in the direction of rotation of said element being substantially vertical, whereby said blades will produce rotation of the fluid suspension as an entire body in said receptacle with minimum agitation of the suspension, and a series of stationary bafiies located within said receptacle, said baflles being spaced at diiferent heights in said receptacle and extending into the spaces between said series of spaced blades, said baffles having faces sloping obliquely upward with respect to the direction of rotation
  • a receptacle for a fluid suspension an element rotated on a substantially vertical axis in said receptacle, means for delivering a diluting liquid to said receptacle, means for delivering the fluid suspension into the lower portion of said receptacle, means for withdrawing the fluid suspension from the upper portion of said receptacle, a series of paddle blades secured to said rotated element, said blades arranged in pairs, the blades in each pair being at the same horizontal level and.
  • a receptacle for a fluid suspension an element rotated on a substantially vertical axis in said receptacle, means for delivering a diluting liquid to said receptacle, means for delivering the fluid suspension into the bottom of said receptacle, means for withdrawing the fluid suspension from the top of said receptacle, a series of paddle blades secured to said rotated element and spaced at difierent heights on said element, the forward faces of said blades in the direction of rotation of said element being substantially vertical, whereby said blades will produce rotation of the fluid suspension as an entire body in said receptacle with minimum agitation of the suspension, a series of stationary baflies located within said receptacle, said bafiles being spaced at different heights in said receptacle and extending into the spaces between said series of spaced blades, said baflles having faces sloping obliquely upward with respect to the direction of rotation of said element to
  • control device character described a receptacle :for a rfiuidxsuspension, ian.:element .rotatedzzonxa substantially verticakaxis said receptacle, :meansdor deliveriing adiluting liquid.

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Description

Jan. 27, 1953 Filed May 5, 1947 L. D. M GLOTHLIN AUTOMATIC CONSISTENCY CONTROL MEANS 2 SHEET$-SHEET l INVENTOR- LEONARD. D. MCGLOTHLIN ATTORN EY 7, 1953 D. M GLQTHLI N AUTOMATIC CONSISTENCY CONTROL MEANS 2 SHEETS-SHEET 2 Filed May 5. 1947 INVENTOR. LEONARD D. MCGLOTHLI N Wag.
AT TOR NEY Patented Jan. 27, 1953 UNITED STATES PATENT OFFICE AUTOMATIC CONSISTENCY CONTROL MEANS This invention relates in general to means employed for regulating the consistency of a fluid suspension by automatically controlling the addition of liquid to the suspension.
In particular, this invention relates to the regulation and control of the consistency of pulp stock, such as that used in the manufacture of paper, especially to stock which has been subjected to cooking in a digester, as, for example, krait paper stock.
After the cooking in the digester the stock is delivered or blown into a tank, commonly referred to as a blow tank, from whence the stock is pumped to the washers in order that the liquor in which the stock has been cooked may be separated from the pulp.
The stock coming from the digester generally has a consistency of about 15%. It is customary to add enough weak liquor to the stock at this stage to reduce the consistency to about 7%, or 6%, so that the stock can be properly handled by the pumps and delivered to the washers. However, as is well known, it is also essential to control the consistency of the stock so that it will be of fairly uniform consistency when delivered to the washers.
An object of the present invention is to provide an improved device for reducing the consistency of the stock, as desired, before the stock is delivered to the washers.
Another object of this invention is to provide an improved control means which will operate automatically and efliciently to maintain a uni-' form predetermined consistency in the stock preparatory to its being pumped to the washers. A further object is to provide an automatic consistency control means which will be highly sensitive to changes in the consistency of the stock and thus able to maintain a more accurate control of the consistency.
An additional object is to provide a consistency control for stock in which black liquor is utilized but in which no excessive foaming of the black liquor will be developed by the control means employed.
The manner in which these objects and other advantages are obtained with my improved consistency control means will be understood from the following description of the construction and operation of the same, in which description reference is made to the accompanying drawings.
In the drawings:
Fig. 1 is a sectional elevation of the main portion of my device with the associated elements of the entire control means indicated more or less diagrammatically;
4 Claims.
Fig. 2 is a plan section taken on line 22 of Fig. 1;
Fig. 3 is a fragmentary view, in perspective,
taken from the interior of the main tank of,
Figs. 1 and 2, showing a portion of the upper rotating paddle and upper baffle in the tank and the outlet from the tank; and
Fig. 4 is a transverse vertical section through one of the bafiies corresponding to line 4-4 of Fig. 2.
Referring first to Figs. 1 and 2, the device includes a main consistency control tank l0, which is preferably cylindrical in shape as indicated. The stock from the digester, after being delivered to the usual blow tank, which is indicated at H in Fig. 1, passes through pipeline l2 into the bottom of the consistency control tank II]. A suitable valve 13, such as a gate valve, is provided in pipeline (2 to control the rate of flow of the stock into tank In or to shut off the flow entirely when desired.
The tank I0 is closed at the top and a stock outlet pipe I4 is connected near the top of tank [0 through which the stock is drawn by pumping means (not shown), and caused to pass to the Washers previously referred to. A clean-out I5 is provided in the bottom of tank l0.
It is customary, in reducing the consistency of stock delivered from the digester, to add weak black liquor to the stock rather than ordinary water. The chief reason for this is that the addi tion of fresh water for the purpose of reducing consistency will dilute the black liquor in the stock and such dilution then hampers the final recovery of the chemicals from the black liquor when the latter has been separated from the pulp as a result of the washing process. Thus, since the consistency of the stock can be reduced by the addition of any liquid, the same general black liquor is used for the purpose.
The weak black liquor which, as mentioned above, is thus used for reducing the consistency of stock in the tank [0, is delivered to the tank I!) by the pipeline l6 through the intermediary of a vertical pipe section I6 which in turn connects with the tank l0 through a plurality of inlet branch pipes indicated at ll, [8 and [9 in Fig. 1. These branch inlet pipes connect with the tank III at difierent levels and each inlet pipe is controlled by a separate hand valve 20. Thus, as apparent from Fig. 1, the incoming diluting liquor can be distributed in equal amounts simultaneously at different levels, as desired, or the comparative rate of distribution at diiferent levels in the tank can be modified. A supplementary inlet port for the liquor is provided at the entrance end of the pipeline I2 between the valve I3 and the tank, this inlet port being shown at 2I in Fig. 1. A branch pipeline (not shown) for the black liquor is connected to this inlet and is also controlled by a suitable hand valve so that the black liquor can be delivered into the bottom of tank In as well as at the other levels, should this ,be desired. Black liquor delivered into the bottom of tank -IU,'when the stock inlet valve I3 is closed, can also be used for flushing out the bottom of the tank I3.
A plurality of baflles 22 extend horizontally within the tank I0. These battles are arranged in pairs at different horizontal levels, as shown in Fig. 1, and the corresponding 'baflies of each pair are arranged in vertical alinement. Thus, as apparent from Fig. 2, these bafiles form two vertical rows. However, these two vertical rows are preferably not diametrically opposite each other. While the baflies extend in horizontal direction, the upper faces of the baffles are inclined so as to form dihedral angles with the horizontal planes in which the lower edges of the baffles lie. The inner end of each baffle 22 is supported by a horizontal brace 23 arranged as shown in Figs. 2, 3 and 4, the inner ends of the braces 23 being connected to the under side of thebailles respectively and the outer ends of the braces being secured to the tank wall a short distance behind the points where the outer. ends of the baflles are secured to the wall.
A vertical shaft 24, centrally located within the tank It), extends upwardly through the tank and through the top of the tank. The bottom end of the shaft 24 is rotatably supported in a suitable bearing 25 located in the bottom of the tank. The shaft .24 extends through a packing box 26 placed on the top of tank I0, and this packing box contains packing gland elements and permits convenient access to the packing gland elements. A gear 21 is secured to the top of the shaft and a suitable thrust bearing is provided between the gear 21 and the top of the packing box 26. A pinion 28, keyed to a horizontal shaft 29, meshes with'gea-r 21. The horizontal shaft 29 is rotatably mounted in a pair of supporting standards 30 which in turn are supported on channel beams extending over the 'top of the tank II]. A sprocket wheel-3| is keyed to the end of the shaft 29' and is driven from a motor 32 through the intermediaryof a reducing unit '33 and sprocket chain connection.
At spaced intervals on the shaft 24, within the tank I0, paddle blades 34 are mounted. These paddle blades are secured to brackets which in turn are rigidly mounted in place on the shaft 24. The paddle blades are arranged in pairs, the forward faces of each pair of blades being substantially diametrically opposite each other as shown in Fig. 2. All the blades are of the same size and shape, each blade preferably having a front face constituting a vertical plane surface and a horizontal reinforcing rib on the rear face. The blades are all arranged so that their front faces will face 'in the direction ofrotation of the entire assembly, thus clock-wise as viewed in Fig. 2.
Unlike the baflies 22, the-respective blades 34 of the pairs are not in vertical alinement but are in staggered vertical sequence. Each pair of blades 34 is placed a short distance below a pair of bafiles 22, as shown in Fig. 1. The upper faces of the baffles 22 are 50 arranged thatthey will engage the stock when rotary motion-isi-mparted to it in one direction by the blades 34 (thus when the stock is rotated clock-wise as viewed in Fig. 2). Thus the entire arrangement of paddles and bafiles is such that as each pair of paddles encounters the stock the paddles will produce a mixing and rotary motion and as the rotating stock encounters each pair of baffles the stock will receive an upward thrust. Consequently the stock will not only be mixed and rotated but will also be moved upwardly from the bottom of the tank until it reaches the outlet pipe I4 through which it is drawn by pump suction. During this 'mixing and lifting of the stock in the tank It] additional liquor is admitted to the stock at various levels and in various amounts in order to lower the consistency of the stock as desired.
The electric power for operating the motor 32, which is used to rotate the paddles 34 in the tank It], is delivered through a thermocouple watt meter, diagrammatically indicated at 35 in Fig. l, which serves to convert wattage to milli-voltage, and which in turn actuates an automatically balancing potentiometer or similar controller, dia grammatically illustrated at 36 in Fig. 1, and this in turn operates a pilot air valve (not shown) controlling the passage of compressed air through the compressed air line 31 to a diaphragm-operated control valve 38 in the pipeline I5. The thermocouple 35, balancing potentiometer and pilot valve 36, and diaphragm valve 38are all well known and of standard construction and need not be further described. The thermocouple 35 and the balancing potentiometer 36, together with the diaphragm valve 38, are so arranged that any load on the motor 32 which exceeds a given minimum will cause the thermocouple watt meter, acting upon the balancing potentiometer which operates the pilot valve in the compressed air line, to permit compressed air to pass to one side of the diaphragm in the diaphragm control valve 38 so as to open the valve 38 against the force of the spring, which spring normally holds the valve closed. This opening of valve 38 permits liquor to pass into the tank I!) through the inlet branch pipes I'I, I8 and I9, as previously mentioned. It will be apparent that the higher the consistency of the stock in the tank ID the greater will be the load on the motor 32, and, similarly, that .the lowering of the consistency of the stock in the tank I!) by the addition of liquor delivered through the inlets I'I, I8 and I9, will reduce the motor load.
The general idea of controlling the dilution or consistency of stock by the amount of power required to rotate a paddle within the stock, is known to be old in the art. However, it will be found that the particular arrangement of paddles, baflies and diluting-liquor inlets which I have provided in my device will greatly facilitate the maintenance of uniformity in the reduced stock consistency. By having a plurality of paddles at different levels, arranged in staggered angular relationship, in combination with the fixed baffles, a slower rate of rotation of the paddles is sufficient for maintaining the consistency control. This is important inasmuch as black liquor has a tendency to foam when agitated too rapidly and the foaming of the liquor gives rise to other subsequent difficulties.
Due to the fact that the stock enters the tank I3 at the bottom and leaves through pipe I4 at the top of the tank, and to the fact that the stock is given only relativelyslow agitation while passing through the tank, any foreign objects, such as bits of metal which may inadvertently have become mixed with the stock, will have a tendency tocollect at the bottom of the tank, from which point they can easily be removed through the cleanout plug l5. This is another incidental advantage of my device.
From Fig. 2 it will be observed that, due to the fact that the baffles 22 of each pair are not diametrically opposite each other, and due to the staggered angular relationship of the different sets of paddle blades 34, no two paddle blades come into Vertical alinement with any of the baiiles simultaneously. The result of this arrangement is that the resistance to the rotation of the shaft 24 is more evenly distributed throughout each complete revolution of the shaft and paddles. In addition to this feature there is the advantage obtained by introducing the diluting liquor simultaneously at different levels into the tank [0. This not only enables a more thorough mixing of the added liquor and stock to take place but also reduces the amount of fluctuation in the resistance to the rotation of the shaft and paddles; Consequently the dilution of the stock as it passes through tank H), the dilution resulting from the addition of extra black liquor required to bring the stock down to the desired predetermined lower consistency, takes place without resulting in any wide range of fluctuation in the load on the motor 32. Excessive fluctuation in the motor load has heretofore been encountered with consistency control devices which similarly regulate the dilution by the motor load. Since the range of fluctuation of the motor load is thus reduced the entire means becomes more sensitive and this greater sensitivity in turn makes possible a closer control and greater uniformity in the consistency of the stock with my invention.
Several modifications in the means which I have described and illustrated would be possible without departing from the main principles of my invention. Thus other arrangements of the plurality of paddles and baffles within the tank It! could be worked out to produce substantially the same results. Consequently it is not my intention to restrict myself to means constructed exactly as illustrated or to limit my invention otherwise than as set forth in the claims. However, the particular means illustrated I regard as a preferred means for carrying out my invention and this same means is proving satisfactory in actual practice.
Although I have described my invention as employed for the purpose of controlling the consistency of certain types of paper stock at a particular stage, and this I consider to be the main field of use for my invention, nevertheless I do not wish to limit my invention to any particular use since the invention could be employed to control the addition of a modifying medium to other fluid suspensions.
I claim:
1. In a consistency control device of the character described, a receptacle for a fluid suspension, an element rotated on a substantially vertical axis in said receptacle, means for delivering a diluting liquid to said receptacle, means for delivering the fluid suspension into the lower portion of said receptacle, means for withdrawing the fluid suspension from the upper portion of said receptacle, a series of paddle blades secured to said rotated element and spaced at different heights on said element, the forward faces of said blades in the direction of rotation of said element being substantially vertical, whereby said blades will produce rotation of the fluid suspension as an entire body in said receptacle with minimum agitation of the suspension, and a series of stationary bafiies located within said receptacle, said baflles being spaced at diiferent heights in said receptacle and extending into the spaces between said series of spaced blades, said baffles having faces sloping obliquely upward with respect to the direction of rotation of said element to promote upward movement of the rotating suspension in said receptacle.
2. In a consistency control device of the character described, a receptacle for a fluid suspension, an element rotated on a substantially vertical axis in said receptacle, means for delivering a diluting liquid to said receptacle, means for delivering the fluid suspension into the lower portion of said receptacle, means for withdrawing the fluid suspension from the upper portion of said receptacle, a series of paddle blades secured to said rotated element, said blades arranged in pairs, the blades in each pair being at the same horizontal level and. extending in substantially diametrically opposite directions, said pairs of blades being spaced at diiferent heights on said element, the forward faces of said blades in the direction of rotation of said element being substantially vertical, whereby said blades will produce rotation of the fluid suspension as an entire body in said receptacle with minimum agitation of the suspension, the corresponding blades at diiferent heights being arranged in staggered relative position, and a series of stationary baffles located within said receptacle, said baffles arranged in pairs, the bailles in each pair being at the same horizontal level but not arranged diametrically opposite each other, said pairs of baffles being spaced at different heights in said receptacle and extending into the spaces between said series of spaced pairs of blades, the corresponding baffles at different heights being in substantially vertical alignment, the arrangement of said blades and baffles being such as to avoid several blades being in vertical alignment with adjacent bafiles at the same instant, thereby reducing fluctuations in the power required for rotating said element, said bafiles having faces sloping obliquely upward with respect to the direction of rotation of said element to promote upward movement of the rotating suspension in said receptacle.
3. In a consistency control device of the character described, a receptacle for a fluid suspension, an element rotated on a substantially vertical axis in said receptacle, means for delivering a diluting liquid to said receptacle, means for delivering the fluid suspension into the bottom of said receptacle, means for withdrawing the fluid suspension from the top of said receptacle, a series of paddle blades secured to said rotated element and spaced at difierent heights on said element, the forward faces of said blades in the direction of rotation of said element being substantially vertical, whereby said blades will produce rotation of the fluid suspension as an entire body in said receptacle with minimum agitation of the suspension, a series of stationary baflies located within said receptacle, said bafiles being spaced at different heights in said receptacle and extending into the spaces between said series of spaced blades, said baflles having faces sloping obliquely upward with respect to the direction of rotation of said element to promote upward movement of the rotating suspension in said receptacle, inlet ports for said diluting liq- 7 uid-spaced-at=diiferentmeightsiin'saidmeceptacle. nds for;controllingzthezpassage nfidilntin liquid through each port into Vsaidmeceptacle.
4. In a consistency "control device; ofbthe: character described a receptacle :for a rfiuidxsuspension, ian.:element .rotatedzzonxa substantially verticakaxis said receptacle, :meansdor deliveriing adiluting liquid. towsaidireceptacle, .means forxdelivering thefiuid suspension .into ithe; bot .tom.pfizsaidaxreceptacla :means for withdrawing the fluid'isuspensionlfrom :the t p of said: receptacle, aseries of: paddle:.-blade s secured to said rotated element, said .blades arranged in pairs, the-blades-in :eachgpair being .at the same horizontal level; and extending in substantially .dlametricallyxopposite'directions, saidjpairsof blades being-.dspaceduat ldifierent heights :on said-relement, theliorwardiaces'of vsaid blades inthe direction pirrotation of said element being'substantially vertical, whereby vsaid blades will pro- .duce:rotation .oithe; fiuidsuspensionas an en- .tireabody in saidreceptacle withiminimum agitationpf the suspension, aseries of stationary baffles located :within said receptacle, said-baffles ,arrangedin "pairs, the baffles in each pair being 1at;the same-horizontal leve1, ;said'pairs of hafiles being.v spaced at differentheights 'iITSaid receptacle. and; extending into the spaces between said;.series .nfiaspaced. pairs of vblades. .1S%id..h&fl18$ 8 havingf'facesrslopin "obliquely-- upward with-re spect; to thexdirectienof rotation ofizsaid element to promote -upward :movement, of the, rotating suspension 'in-said; receptacle, inlet ports for said diluting liquid spaced at different heights in said receptacle, and means for relatively controlling the passageiof diluting liquid 'throughzeach; port into saidH-receptacle.
LEONARD D. ,JMCGLOTHLIN.
REFERENCES CITED The following references are of record initthe file of this patent:
ITED. iSTATES"PATENTS
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US2694688A (en) * 1953-02-27 1954-11-16 Du Pont Antistatic compositions for textiles
US2746729A (en) * 1952-08-05 1956-05-22 Pittsburgh Plate Glass Co Method for homogenizing glass
US2806298A (en) * 1951-07-17 1957-09-17 Rossi Giovanni Process and device for the treatment of substances in small pieces, by means of a fluid
US2852348A (en) * 1954-04-05 1958-09-16 Babcock & Wilcox Co Apparatus for preparing residual liquor
US2904401A (en) * 1955-11-01 1959-09-15 Wallace & Tiernan Inc Viscosity control method and apparatus for hydrating lime
US2908652A (en) * 1955-08-15 1959-10-13 Forrester Gilbert Process and apparatus for defoaming liquids
US2924439A (en) * 1957-05-27 1960-02-09 Du Pont Apparatus for making dispersions
US2953460A (en) * 1950-08-03 1960-09-20 Baker Process Company Process and apparatus for preparing dough
US2957339A (en) * 1957-03-22 1960-10-25 Penny Francis David Viscometer
US2972546A (en) * 1957-03-08 1961-02-21 Eastman Kodak Co Method and apparatus for manufacturing colored sheeting
US3023175A (en) * 1957-10-09 1962-02-27 Koppers Co Inc Process and apparatus for the preexpansion of vinyl polymeric materials
US3036214A (en) * 1955-11-29 1962-05-22 Du Pont Viscosity determination
US3266874A (en) * 1963-04-02 1966-08-16 Phillips Petroleum Co Agglomerating carbon black by maintaining constant pelletizer motor power requirement
US3266873A (en) * 1963-04-01 1966-08-16 Phillips Petroleum Co Carbon black pelleting by controlling power to the pelletizer motor
US3269171A (en) * 1964-06-19 1966-08-30 Herbert K Bruss Apparatus for measuring the viscosity of liquid and plastic materials
US3317435A (en) * 1963-05-23 1967-05-02 Ajinomoto Kk Method for feeding an anti-foaming agent to a reaction vessel
US3347529A (en) * 1955-08-08 1967-10-17 Bayer Ag Apparatus for the manufacture of polyurethane plastics
US3615243A (en) * 1969-05-22 1971-10-26 Clarence W Scott Apparatus for extracting liquid from a mobile semisolid cellular system
US3638673A (en) * 1969-12-23 1972-02-01 Lampcraft Tool & Mold Inc Wax-conditioning apparatus
US3770386A (en) * 1968-04-02 1973-11-06 Kureha Chemical Ind Co Ltd Apparatus for purifying crystals comprising a stirrer with fins forming a discontinuous spiral
US4155657A (en) * 1978-03-10 1979-05-22 Chemed Corporation Continuous mixer for preparing emulsions
US4189240A (en) * 1979-01-31 1980-02-19 Toledo Stamping & Manufacturing Company Mixer for animal feed
US4283938A (en) * 1978-10-09 1981-08-18 Klockner-Humboldt-Deutz Ag Method and apparatus for dynamic concentration of a suspension
US4622846A (en) * 1985-11-05 1986-11-18 Halliburton Company Consistency and static gel strength measuring device and method
US4653313A (en) * 1985-10-18 1987-03-31 Halliburton Company Positive stirring consistometer cup and method of using the same
US4680957A (en) * 1985-05-02 1987-07-21 The Davey Company Non-invasive, in-line consistency measurement of a non-newtonian fluid
US4823594A (en) * 1988-03-14 1989-04-25 Halliburton Company Container for a fluid to be tested under pressure
US4948440A (en) * 1987-10-05 1990-08-14 C-I-L Inc. Emulsion blasting agent preparation system
US5353827A (en) * 1991-11-18 1994-10-11 Chandelles Tradition Candle Ltee Process for producing pasty paraffin
US5362149A (en) * 1990-03-16 1994-11-08 Nelson Richard J Vortex finder high shear mud mixing system
US5393138A (en) * 1990-03-05 1995-02-28 Federhen; Bernd Apparatus for mixing foundry mould substances
US5470153A (en) * 1993-02-12 1995-11-28 Machines Collette Mixing device for aerating and mixing pumpable semi-liquid products
US20040149019A1 (en) * 2003-01-30 2004-08-05 Johnson Johnny W. Yield point adaptation for rotating viscometers
US6782735B2 (en) 2000-02-08 2004-08-31 Halliburton Energy Services, Inc. Testing device and method for viscosified fluid containing particulate material
US20070079961A1 (en) * 2005-10-07 2007-04-12 Halliburton Energy Services, Inc. Proppant suspension testing devices and methods of use
US20080037361A1 (en) * 2006-02-15 2008-02-14 Jerry Fleishman Mixer apparatus
US20080089987A1 (en) * 2006-10-12 2008-04-17 Horn Darrell C Continuous Intermeshing Agitator Food Cooker
US20100004890A1 (en) * 2008-07-02 2010-01-07 Halliburton Energy Services, Inc. Device and method for testing friction reduction efficiency and suspension systems
US20100018294A1 (en) * 2008-07-28 2010-01-28 Halliburton Energy Services, Inc. Flow-through apparatus for testing particle laden fluids and methods of making and using same
US20110140858A1 (en) * 1998-04-24 2011-06-16 Ovard David K Methods and apparatus for rfid tag communications
US8347693B2 (en) 2010-08-26 2013-01-08 Halliburton Energy Services, Inc. Apparatus and methods for continuous compatibility testing of subterranean fluids and their compositions under wellbore conditions
US20150016211A1 (en) * 2013-07-09 2015-01-15 Wenger Manufacturing, Inc. Steam/water static mixer injector for extrusion equipment
US20150290608A1 (en) * 2012-12-07 2015-10-15 Cidra Corporate Services Inc. Techniques for agglomerating mature fine tailing by injecting a polymer in a process flow

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Cited By (55)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2953460A (en) * 1950-08-03 1960-09-20 Baker Process Company Process and apparatus for preparing dough
US2806298A (en) * 1951-07-17 1957-09-17 Rossi Giovanni Process and device for the treatment of substances in small pieces, by means of a fluid
US2746729A (en) * 1952-08-05 1956-05-22 Pittsburgh Plate Glass Co Method for homogenizing glass
US2694688A (en) * 1953-02-27 1954-11-16 Du Pont Antistatic compositions for textiles
US2852348A (en) * 1954-04-05 1958-09-16 Babcock & Wilcox Co Apparatus for preparing residual liquor
US3347529A (en) * 1955-08-08 1967-10-17 Bayer Ag Apparatus for the manufacture of polyurethane plastics
US2908652A (en) * 1955-08-15 1959-10-13 Forrester Gilbert Process and apparatus for defoaming liquids
US2904401A (en) * 1955-11-01 1959-09-15 Wallace & Tiernan Inc Viscosity control method and apparatus for hydrating lime
US3036214A (en) * 1955-11-29 1962-05-22 Du Pont Viscosity determination
US2972546A (en) * 1957-03-08 1961-02-21 Eastman Kodak Co Method and apparatus for manufacturing colored sheeting
US2957339A (en) * 1957-03-22 1960-10-25 Penny Francis David Viscometer
US2924439A (en) * 1957-05-27 1960-02-09 Du Pont Apparatus for making dispersions
US3023175A (en) * 1957-10-09 1962-02-27 Koppers Co Inc Process and apparatus for the preexpansion of vinyl polymeric materials
US3266873A (en) * 1963-04-01 1966-08-16 Phillips Petroleum Co Carbon black pelleting by controlling power to the pelletizer motor
US3266874A (en) * 1963-04-02 1966-08-16 Phillips Petroleum Co Agglomerating carbon black by maintaining constant pelletizer motor power requirement
US3317435A (en) * 1963-05-23 1967-05-02 Ajinomoto Kk Method for feeding an anti-foaming agent to a reaction vessel
US3269171A (en) * 1964-06-19 1966-08-30 Herbert K Bruss Apparatus for measuring the viscosity of liquid and plastic materials
US3770386A (en) * 1968-04-02 1973-11-06 Kureha Chemical Ind Co Ltd Apparatus for purifying crystals comprising a stirrer with fins forming a discontinuous spiral
US3615243A (en) * 1969-05-22 1971-10-26 Clarence W Scott Apparatus for extracting liquid from a mobile semisolid cellular system
US3638673A (en) * 1969-12-23 1972-02-01 Lampcraft Tool & Mold Inc Wax-conditioning apparatus
US4155657A (en) * 1978-03-10 1979-05-22 Chemed Corporation Continuous mixer for preparing emulsions
US4283938A (en) * 1978-10-09 1981-08-18 Klockner-Humboldt-Deutz Ag Method and apparatus for dynamic concentration of a suspension
US4189240A (en) * 1979-01-31 1980-02-19 Toledo Stamping & Manufacturing Company Mixer for animal feed
US4680957A (en) * 1985-05-02 1987-07-21 The Davey Company Non-invasive, in-line consistency measurement of a non-newtonian fluid
US4653313A (en) * 1985-10-18 1987-03-31 Halliburton Company Positive stirring consistometer cup and method of using the same
US4622846A (en) * 1985-11-05 1986-11-18 Halliburton Company Consistency and static gel strength measuring device and method
US4948440A (en) * 1987-10-05 1990-08-14 C-I-L Inc. Emulsion blasting agent preparation system
US4823594A (en) * 1988-03-14 1989-04-25 Halliburton Company Container for a fluid to be tested under pressure
US5393138A (en) * 1990-03-05 1995-02-28 Federhen; Bernd Apparatus for mixing foundry mould substances
US5362149A (en) * 1990-03-16 1994-11-08 Nelson Richard J Vortex finder high shear mud mixing system
US5353827A (en) * 1991-11-18 1994-10-11 Chandelles Tradition Candle Ltee Process for producing pasty paraffin
US5470153A (en) * 1993-02-12 1995-11-28 Machines Collette Mixing device for aerating and mixing pumpable semi-liquid products
US20110140858A1 (en) * 1998-04-24 2011-06-16 Ovard David K Methods and apparatus for rfid tag communications
US8855169B2 (en) 1998-04-24 2014-10-07 Round Rock Research, Llc Methods and apparatus for RFID tag communications
US6782735B2 (en) 2000-02-08 2004-08-31 Halliburton Energy Services, Inc. Testing device and method for viscosified fluid containing particulate material
US6874353B2 (en) 2003-01-30 2005-04-05 Halliburton Energy Services, Inc. Yield point adaptation for rotating viscometers
US20040149019A1 (en) * 2003-01-30 2004-08-05 Johnson Johnny W. Yield point adaptation for rotating viscometers
US7392842B2 (en) * 2005-10-07 2008-07-01 Halliburton Energy Services, Inc. Proppant suspension testing devices and methods of use
US20070079961A1 (en) * 2005-10-07 2007-04-12 Halliburton Energy Services, Inc. Proppant suspension testing devices and methods of use
US20080037361A1 (en) * 2006-02-15 2008-02-14 Jerry Fleishman Mixer apparatus
US20080089987A1 (en) * 2006-10-12 2008-04-17 Horn Darrell C Continuous Intermeshing Agitator Food Cooker
US20100004890A1 (en) * 2008-07-02 2010-01-07 Halliburton Energy Services, Inc. Device and method for testing friction reduction efficiency and suspension systems
US7992427B2 (en) 2008-07-02 2011-08-09 Halliburton Energy Services Inc., Device and method for testing friction reduction efficiency and suspension systems
US20100018294A1 (en) * 2008-07-28 2010-01-28 Halliburton Energy Services, Inc. Flow-through apparatus for testing particle laden fluids and methods of making and using same
US8024962B2 (en) 2008-07-28 2011-09-27 Halliburton Energy Services Inc. Flow-through apparatus for testing particle laden fluids and methods of making and using same
US8347693B2 (en) 2010-08-26 2013-01-08 Halliburton Energy Services, Inc. Apparatus and methods for continuous compatibility testing of subterranean fluids and their compositions under wellbore conditions
US20150290608A1 (en) * 2012-12-07 2015-10-15 Cidra Corporate Services Inc. Techniques for agglomerating mature fine tailing by injecting a polymer in a process flow
US10071352B2 (en) * 2012-12-07 2018-09-11 Cidra Corporate Services Inc. Techniques for agglomerating mature fine tailing by injecting a polymer in a process flow
US20150016211A1 (en) * 2013-07-09 2015-01-15 Wenger Manufacturing, Inc. Steam/water static mixer injector for extrusion equipment
US9713893B2 (en) * 2013-07-09 2017-07-25 Wenger Manufacturing, Inc. Method of preconditioning comestible materials using steam/water static mixer
US9776355B1 (en) * 2013-07-09 2017-10-03 Wenger Manufacturing, Inc. Extruder with static mixer injector
US9776356B1 (en) * 2013-07-09 2017-10-03 Wenger Manufacturing, Inc. Method of extruder operation using static mixer injector
US20170297249A1 (en) * 2013-07-09 2017-10-19 Wenger Manufacturing, Inc. Method of extruder operation using static mixer injector
US9908090B2 (en) * 2013-07-09 2018-03-06 Wenger Manufacturing, Inc. Steam/water static mixer injector for preconditioners
US9981416B1 (en) * 2013-07-09 2018-05-29 Wenger Manufacturing, Inc. Extruder with static mixer injector

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