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US3881654A - Battery paste pumping and metering system - Google Patents

Battery paste pumping and metering system Download PDF

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Publication number
US3881654A
US3881654A US421304A US42130473A US3881654A US 3881654 A US3881654 A US 3881654A US 421304 A US421304 A US 421304A US 42130473 A US42130473 A US 42130473A US 3881654 A US3881654 A US 3881654A
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Prior art keywords
paste
pump
closed loop
flow
nozzle
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US421304A
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Terrance M Larkin
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Gates Rubber Co
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Gates Rubber Co
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/14Electrodes for lead-acid accumulators
    • H01M4/16Processes of manufacture
    • H01M4/20Processes of manufacture of pasted electrodes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B9/00Spraying apparatus for discharge of liquids or other fluent material, without essentially mixing with gas or vapour
    • B05B9/03Spraying apparatus for discharge of liquids or other fluent material, without essentially mixing with gas or vapour characterised by means for supplying liquid or other fluent material
    • B05B9/04Spraying apparatus for discharge of liquids or other fluent material, without essentially mixing with gas or vapour characterised by means for supplying liquid or other fluent material with pressurised or compressible container; with pump
    • B05B9/0403Spraying apparatus for discharge of liquids or other fluent material, without essentially mixing with gas or vapour characterised by means for supplying liquid or other fluent material with pressurised or compressible container; with pump with pumps for liquids or other fluent material
    • B05B9/0406Spraying apparatus for discharge of liquids or other fluent material, without essentially mixing with gas or vapour characterised by means for supplying liquid or other fluent material with pressurised or compressible container; with pump with pumps for liquids or other fluent material with several pumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05CAPPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05C5/00Apparatus in which liquid or other fluent material is projected, poured or allowed to flow on to the surface of the work
    • B05C5/02Apparatus in which liquid or other fluent material is projected, poured or allowed to flow on to the surface of the work the liquid or other fluent material being discharged through an outlet orifice by pressure, e.g. from an outlet device in contact or almost in contact, with the work
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C13/00Adaptations of machines or pumps for special use, e.g. for extremely high pressures
    • F04C13/001Pumps for particular liquids
    • F04C13/002Pumps for particular liquids for homogeneous viscous liquids
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • This invention relates to systems for pasting battery plates, and particularly to such systems which are required to handle highly viscous, thixotropic, slurry-like suspensions of discrete crystalline finely divided particles.
  • the present invention includes a system and cally active paste onto a suitable electrode substrate.
  • the system comprises a closed loop conduit system connecting a circulating pump, fed through an inlet reservoir, with a pumping/metering device for initiating flow of a portion of the circulating paste and for metering a predetermined volumetric flow rate of the paste to a discharge nozzle, or the like.
  • Paste consistency and working life are enhanced by the mixing effect of repeated passes of the paste through the pumps in the closed loop system.
  • the speed of the traveling substrate may be chosen so that uniform pasting of the grid is effected without waste of paste and without the use of doctor blades or other controlling devices.
  • FIG. I is a flow diagram of the overall paste pumping and metering system of the invention.
  • FIG. 2 shows a fragmentary partial sectional view of the forward portion of a preferred type of positive displacement pump denoted either as pump II or pump 13 of FIG. 1',
  • FIG. 3 is an end view at the outlet ofa discharge nozzle useful in the invention
  • FIGS. 4, 5, and 6 are different sectional views of the nozzle of FIG. 3 taken along the designated sections;
  • FIG. 7 is an end view at the outlet of another type of nozzle useful in the present invention.
  • FIGS. 8, 9 and 10 depict various sectional views of the nozzle of FIG. 7 taken along the sections as shown.
  • a closed loop pumping, circulating, and battery paste metering system generally includes a circulating pump 13 and metering pump I] connected through forward conduit 15 and return conduit I7.
  • Battery paste is charged to the closed loop through an inlet means such as reservoir 19 provided with a biasing means for applying a net positive suction head to the circulating pump 13, and discharged through conduit 18 and nozzle 12 onto electrode substrate 14.
  • This biasing means at the inlet side may be selected from a number of suitable devices well known and appreciated by those skilled in the art. Examples include piston ram 2] provided with a weight 23, a spring, dead weight, fluid pressure head or rolling dia phragm membrane.
  • the biasing means preferably isolates the battery paste from exposure to the atmosphere to preclude possible degradation.
  • the litharge particles preferably are discrete crystalline finely divided solids of a ceramic nature of macroscopic size. Oftentimes additional paste constitutents, such as an expander, lead and Pb O are present. It is preferred that the battery paste contain no entrained fluids which may have the effect of degrading the paste by oxidation or other mechanism.
  • the meshing helical surfaces push the battery paste ahead along the progressing cavities 29 with uniform movement and low turbulence similar to a slow moving piston in a cylinder of infinite length.
  • the screw-like roter rolls within the nut-like stator with an eccentric rolling movement.
  • the speed of the roter 25 and hence the rate of flow of the paste within the closed loop may be varied according to the output speed of a variable speed drive pump motor 31.
  • a passive mechanism eg. a three-way valve
  • a three-way valve has been found to be ineffective insomuch as the valve is incapable of diverting and initiating flow of a particular desired por tion of the circulating paste away from the closed loop without eventual plugging, channeling and stoppage.
  • a positive displacement metering pump 11 is required.
  • This pump may suitably be driven by a motor 16 whose speed is preferably directly proportional to the speed of the battery substrate material 14 as it passes beneath and in close proximity to the discharge nozzle I2.
  • This positive displacement metering pump 11 may be of various types although the archimedes' screw type, exemplified by the aforementioned MOYNO type, is preferred.
  • the volumetric flow rate of paste to the discharge means 12 may be controlled within any desired range. This capability holds virtually independent of temperature and the internal pressure of the paste exerted within the closed loop, provided a net positive suction head exists at the pump inlet and the pump has not cavitated.
  • the relative speeds of the two pumps are chosen so that only a desired proportion of the circulating paste is diverted to the discharge means 12.
  • the ratio of the amount of paste allowed to recirculate in the closed loop to the amount of paste material metered to the discharge means is preferably from about 50:l to about 15:1. and more preferably from about 30:1 to about 20:].
  • the discharge means 12 is preferably in the configuration of a nozzle whose geometry is designed to accommodate substantially unobstructed flow of the viscous, thixotropic paste.
  • One embodiment of the discharge means includes a depending nozzle 12 which conducts fluid from the metering pump 11 through curved conduit 18.
  • the head of the nozzle 12 preferably has a tapered surface 19 which is arranged substantially parallel to the moving substrate material 14. In the instance where the substrate material is of a soft and deformable nature (cg. high purity expanded lead mesh) it is preferred to position the surface 19 slightly above the moving substrate. In this manner, the nozzle acts similarly in function to a doctor blade without deforming the substrate 14.
  • a soft and deformable nature cg. high purity expanded lead mesh
  • Preferred nozzle configurations are those which convert a substantially cylindrical input flow from the positive displacement pump to a ribbon-like rectangular output for application to the substrate. Because of the rheology of the paste composition, traditional nozzle structures have not been found workable insomuch as the paste has tended to cling to the interior surfaces of the nozzle, allowing the paste to be discharged only through the central portions of the nozzle, a phenomenon commonly known as channeling.
  • FIGS. 3-6 Two types of nozzle configurations can effectively accommodate such a viscous non- Newtonian fluid after hours of continuous use without significant channeling.
  • the first type is depicted in FIGS. 3-6 in which substantially straight nozzle sides 31 are employed in the transition from the cylindrical or circular input 33 to the substantially rectangular output 35.
  • this first embodiment having straight sides 31 it is important that the cross-sectional area of the interior of the nozzle, such as noted by the reference numeral 37 in FIG. 6, increases essentially monotonically from the inlet point 33 to the outlet point 35.
  • the second type of nozzle configuration is shown in FIGS. 7-10 and employs a constant or substantially constant cross-sectional area as a progression is made from the cylindrical inlet 41 to the rectangular-like outlet 43.
  • a substantially constant crosssectional area it is important that the internal fluid flow surfaces 45 of the nozzle as shown in FIG. 8 be substantially diverted or curved outwardly, apparently to minimize boundary frictional force which seem to predominate over internal paste shear forces.
  • this curved surface 45 is a portion of or substan tially resembles a portion of one of the conic sections, as viewed perpendicularly to the direction of fluid flow and to the length of rectangle-like surface 43.
  • cross-sectional area 39 contains inwardly curved depressions 47 to further inhibit boundary frictional problems which might lead to channeling.
  • the outlet slit 43 also preferably contains centrally located slight depressions 47' to prevent channeling. It is believed that those skilled in the art will appreciate additional nozzle configurations useful and within the scope of the present invention.
  • thermosetting polymeric materials such as cast epoxy or polyester resins or machined acrylic have been found suitable.
  • a substantially closed loop system for pumping and metering viscous thixotropic electrochemically active paste through a discharge means comprising:
  • first pump means for agitating and circulating said paste around the loop
  • second pump means downstream of said first pump means, for initiating flow of a portion of the circulating paste away from the closed loop to the discharge means; said second pump means metering a predetermined volumetric flow rate of paste to said discharge means.
  • said inlet means comprises a reservoir, battery paste within the reservoir, and biasing means applying a net positive suction head urging said battery paste to enter said closed loop.
  • said first pump means is a positive displacement pump of the archimedes screw type.
  • said second pump means is a positive displacement pump of the archimedes screw type containing a metering valve.
  • said discharge means comprises a nozzle which converts a substantially cylindrical input flow from said second pump means to a substantially rectangular output flow for uniform delivery to a moving substrate.
  • a source of highly viscous non-plastic thixotropic battery paste comprising a major proportion of oxides of lead suspended in a minor proportion of aqueous vehicle
  • inlet means for charging make-up thixotropic paste to said closed loop system
  • first pump means for agitating and circulating said paste around the loop
  • second pump means in connection with said discharge means, downstream of said first pump means, for initiating flow of a portion of the circulating paste away from the closed loop to the dis charge means;
  • said second pump means metering a predetermined volumetric flow rate of paste to said discharge means which is in turn metered to the substrate at the predetermined volumetric flow rate.
  • said discharge means comprises a nozzle which converts a substantially cylindrical input flow from said second pump means to a substantially rectangular output flow for uniform delivery to the substrate.
  • outlet portion is substantially parallel to the surface formed by the substrate onto which the paste is to be deposited.

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Coating Apparatus (AREA)

Abstract

A closed loop pumping and metering system for pasting battery electrode plates with a viscous, thixotropic battery paste is disclosed. The closed loop includes an inlet for charging make-up paste, a first pump for agitating and circulating the paste around the loop, and a metering pump downstream of the circulating pump for initiating flow of a predetermined volumetric flow rate of paste through a discharge means onto a battery grid substrate, or the like. The paste consistency and working life are enhanced by the mixing effect provided by repeated passes through the circulating and metering pumps.

Description

United States Patent 11 1 1111 3,881,654 Larkin May 6, 1975 [5 1 BATTERY PASTE PUMPING AND 3.023.968 3/1962 Mitchell 239/142 x METERING SYSTEM 3,203,631 8/l965 Jutila .1 239/142 X 3,49l 949 1/1970 Hairston 1 4 i 239/142 X Inventor: Terrance M a Littlewn, 3,716.066 2/1973 Currier et al. 1, 239 142 x C010. 3,808,040 4/1974 Barnes et a1. .1 1 [7/44 X [73] Assignee: The Gates Rubber Company, FOREIGN PATENTS OR APPLICATIONS Dem. 608,576 9/l948 United Kingdom 239 127 Dec. 3, 624,255 6/1949 UflllCd Kingdomm, 136/19 126,471 1919 Umted K1ngd0m...,............. 239/592 [21] Appl. No.: 421,304
Related [1.8. Application Data :rimary j l f c tw lg c 'fl J Itorney, gent, or 1rmur 1s as eman. r.; 62 D f S N 244,485, A l 17, 1972, P' I N 3 fiz 1zs2s o Raymond Flnk; H. w. Oberg. Jr.
52 us. (:1. 239/127; 239/142; 239/597; 15 1 ABSTRACT 239/60]; 117/44; 136/19 A closed loop pumping and metering system for past- 1 1 '3 Bosh 9/00; 505C 1/16; Holm 35/00 ing battery electrode plates with a viscous, thixotropic [58] of Search 117/20l- 43, battery paste is disclosed. The closed loop includes an 1 17/1051; 136/19 33; 239/592, inlet for charging make-up paste, a first pump for agi- 123, 597, 6 118/410 tating and circulating the paste around the loop, and a metering pump downstream of the circulating pump 156] References and for initiating flow of a predetermined volumetric flow UNITED STATES PATENTS rate of paste through a discharge means onto a battery 1,630,974 5/1927 Shelor et a1 239 597 x grid substrate, or the like- The pasts consistency and 2,166,300 7/1939 K r H 239/592 X working life are enhanced by the mixing effect pro- 2,599,604 6/1952 Bauer et aL. 117/44 vided by repeated passes through the circulating and 2,636,780 4/1953 Barnes i 239/594 X metering pumps 2,879,003 3 1959 Finn 239/592 x 2,983,286 6 1961 Snyder et a1 239 142 x 22 Chums, 10 Drawlfls Figures 23 ll l2 SHEET 2 BF 2 FIGS BATTERY PASTE PUMPING AND METERING SYSTEM This is a division of application Ser. No. 244,485, filed Apr. l7, I972, now U.S. Pat. No. 3,8l4,628.
BACKGROUND OF THE INVENTION This invention relates to systems for pasting battery plates, and particularly to such systems which are required to handle highly viscous, thixotropic, slurry-like suspensions of discrete crystalline finely divided particles.
In the assembly production of pasted battery plates, it has been common to pump the paste through a discharge means, such as a nozzle, with an open feed gear pump onto a moving grid, expanded mesh, or other type of conductive substrate. In such a system, it has been a common characteristic for a non-uniform volumetric flow rate of paste to be discharged upon the moving substrate, requiring the use of doctor blades or other means to scrape off the excess paste. This often results in the waste of paste, the non-uniform deposition of paste, and in the case where the substrate is of a non-grid character the deformation or flattening of the soft substrate by the doctor blade. These drawbacks are magnified when the paste is highly viscous, thixotropic, and resembles a slurry or suspension of fine solid particles in a vehicle. Such paste may rheologically resemble quick clays," wet mortar, cement, or the like. The finely divided particles of solids are generally macromolecular in size, rather than colloidal. These paste materials are essentially non-plastic and behave like non-Newtonian fluids insomuch as the viscosity of the paste varies with its rate of flow in the closed loop network. As such, significant problems are encountered in circulating and metering a predetermined amount of the paste at a given flow rate onto a passing substrate and in avoiding setting up of the paste.
Traditional systems for circulating common thixotropic types of materials, such as shown in U.S. Pat. No. 2,65l,586 (Cooper et a1.) employ a circulating pump in series with a type of constant pressure aided three way valve for intermittent metering of the material. Such a valve type of metering device has been tested and found to be ineffective for discharging at a predetermined flow rate highly viscous, non-Newtonian fluids such as contemplated by the present invention. The general state of the art is also exemplified by the teachings of U.S. Pat. Nos. 2,479,603 (Chubb et al.), 2,972,546 (Adler et al.), and 3,529,626 (German).
SUMMARY OF THE INVENTION Briefly, the present invention includes a system and cally active paste onto a suitable electrode substrate. The system comprises a closed loop conduit system connecting a circulating pump, fed through an inlet reservoir, with a pumping/metering device for initiating flow of a portion of the circulating paste and for metering a predetermined volumetric flow rate of the paste to a discharge nozzle, or the like. Paste consistency and working life are enhanced by the mixing effect of repeated passes of the paste through the pumps in the closed loop system. By discharging a substantially constant flow rate of paste, the speed of the traveling substrate may be chosen so that uniform pasting of the grid is effected without waste of paste and without the use of doctor blades or other controlling devices.
BRIEF DESCRIPTION OF THE DRAWINGS The invention will be more particularly set forth in various of its embodiments by reference to the accompanying drawings, in which:
FIG. I is a flow diagram of the overall paste pumping and metering system of the invention;
FIG. 2 shows a fragmentary partial sectional view of the forward portion of a preferred type of positive displacement pump denoted either as pump II or pump 13 of FIG. 1',
FIG. 3 is an end view at the outlet ofa discharge nozzle useful in the invention;
FIGS. 4, 5, and 6 are different sectional views of the nozzle of FIG. 3 taken along the designated sections;
FIG. 7 is an end view at the outlet of another type of nozzle useful in the present invention; and
FIGS. 8, 9 and 10 depict various sectional views of the nozzle of FIG. 7 taken along the sections as shown.
PREFERRED EMBODIMENTS OF THE INVENTION Referring to FIG. I, a closed loop pumping, circulating, and battery paste metering system generally includes a circulating pump 13 and metering pump I] connected through forward conduit 15 and return conduit I7. Battery paste is charged to the closed loop through an inlet means such as reservoir 19 provided with a biasing means for applying a net positive suction head to the circulating pump 13, and discharged through conduit 18 and nozzle 12 onto electrode substrate 14. This biasing means at the inlet side may be selected from a number of suitable devices well known and appreciated by those skilled in the art. Examples include piston ram 2] provided with a weight 23, a spring, dead weight, fluid pressure head or rolling dia phragm membrane. The biasing means preferably isolates the battery paste from exposure to the atmosphere to preclude possible degradation.
The rheological nature of the battery paste circulated within the system has been described hereinabove as being highly viscous, thixotropic and exhibiting non- Newtonian character. While viscosity measurements on a Brookfield viscosimeter of the battery paste are not too meaningful for non-Newtonian fluids, apparent viscosity readings of typical battery paste compositions of the invention will often be at least about 3 million centipoises, and quite often greater than about 7 million centipoises. Examples of such paste compositions include negative and positive lead-acid battery pastes which comprise a major proportion of oxides of lead, e.g. litharge, suspended in a minor proportion of a vehicle, e.g. water. The litharge particles preferably are discrete crystalline finely divided solids of a ceramic nature of macroscopic size. Oftentimes additional paste constitutents, such as an expander, lead and Pb O are present. It is preferred that the battery paste contain no entrained fluids which may have the effect of degrading the paste by oxidation or other mechanism.
* Measured with a TF hclipath spindle at 1 rpm. after at least one and up to minutes elapsed time.
In order to circulate such cement-like pastes about a closed loop, circulating pump I3 is preferably of the positive displacement type, exemplified by a diaphragm pump or archimedes screw type pump. This latter type of pump (preferred for lead-acid pastes) is exemplified by the MOYNO pumps (a registered trademark of the Robbins and Myers Corporation) utilizing a progressing cavity arrangement as shown partially in FIG. 2. The operating principle of the pump is based on two pumping elements consisting of a helical roter 25 turning within a double threaded helical stator 27. The meshing helical surfaces push the battery paste ahead along the progressing cavities 29 with uniform movement and low turbulence similar to a slow moving piston in a cylinder of infinite length. The screw-like roter rolls within the nut-like stator with an eccentric rolling movement. The speed of the roter 25 and hence the rate of flow of the paste within the closed loop may be varied according to the output speed of a variable speed drive pump motor 31.
It has been found that in order to achieve uniform deposition of battery paste from the nozzle 12 onto a suitable electrode substrate 14, such as an expanded mesh grid or perforated sheet, more than just a passive mechanism (eg. a three-way valve) is required to meter a predetermined volumetric flow rate of paste to the discharge nozzle l2. A three-way valve has been found to be ineffective insomuch as the valve is incapable of diverting and initiating flow of a particular desired por tion of the circulating paste away from the closed loop without eventual plugging, channeling and stoppage. In order to divert and initiate flow of the desired amount of paste away from the circulating loop represented in part by conduits 15 and 17, a positive displacement metering pump 11 is required. This pump may suitably be driven by a motor 16 whose speed is preferably directly proportional to the speed of the battery substrate material 14 as it passes beneath and in close proximity to the discharge nozzle I2. This positive displacement metering pump 11 may be of various types although the archimedes' screw type, exemplified by the aforementioned MOYNO type, is preferred. By varying the speed of the roter within the pump by means of motor 16, the volumetric flow rate of paste to the discharge means 12 may be controlled within any desired range. This capability holds virtually independent of temperature and the internal pressure of the paste exerted within the closed loop, provided a net positive suction head exists at the pump inlet and the pump has not cavitated.
Because paste consistency and working life are enhanced by the mixing of paste provided by repeated passes through the pumps II and 13, the relative speeds of the two pumps are chosen so that only a desired proportion of the circulating paste is diverted to the discharge means 12. Normally, the ratio of the amount of paste allowed to recirculate in the closed loop to the amount of paste material metered to the discharge means is preferably from about 50:l to about 15:1. and more preferably from about 30:1 to about 20:].
The discharge means 12 is preferably in the configuration of a nozzle whose geometry is designed to accommodate substantially unobstructed flow of the viscous, thixotropic paste. One embodiment of the discharge means includes a depending nozzle 12 which conducts fluid from the metering pump 11 through curved conduit 18. The head of the nozzle 12 preferably has a tapered surface 19 which is arranged substantially parallel to the moving substrate material 14. In the instance where the substrate material is of a soft and deformable nature (cg. high purity expanded lead mesh) it is preferred to position the surface 19 slightly above the moving substrate. In this manner, the nozzle acts similarly in function to a doctor blade without deforming the substrate 14. Those skilled in the art will appreciate the use of other discharge means suitable for applying the paste onto an electrode substrate.
Preferred nozzle configurations are those which convert a substantially cylindrical input flow from the positive displacement pump to a ribbon-like rectangular output for application to the substrate. Because of the rheology of the paste composition, traditional nozzle structures have not been found workable insomuch as the paste has tended to cling to the interior surfaces of the nozzle, allowing the paste to be discharged only through the central portions of the nozzle, a phenomenon commonly known as channeling.
It has been found that two types of nozzle configurations can effectively accommodate such a viscous non- Newtonian fluid after hours of continuous use without significant channeling. The first type is depicted in FIGS. 3-6 in which substantially straight nozzle sides 31 are employed in the transition from the cylindrical or circular input 33 to the substantially rectangular output 35. In this first embodiment having straight sides 31, it is important that the cross-sectional area of the interior of the nozzle, such as noted by the reference numeral 37 in FIG. 6, increases essentially monotonically from the inlet point 33 to the outlet point 35.
The second type of nozzle configuration is shown in FIGS. 7-10 and employs a constant or substantially constant cross-sectional area as a progression is made from the cylindrical inlet 41 to the rectangular-like outlet 43. To maintain such a substantially constant crosssectional area, it is important that the internal fluid flow surfaces 45 of the nozzle as shown in FIG. 8 be substantially diverted or curved outwardly, apparently to minimize boundary frictional force which seem to predominate over internal paste shear forces. Preferably this curved surface 45 is a portion of or substan tially resembles a portion of one of the conic sections, as viewed perpendicularly to the direction of fluid flow and to the length of rectangle-like surface 43. It is also preferred that while progressing from the inlet point 41 to the outlet point 43 that cross-sectional area 39 contains inwardly curved depressions 47 to further inhibit boundary frictional problems which might lead to channeling. The outlet slit 43 also preferably contains centrally located slight depressions 47' to prevent channeling. It is believed that those skilled in the art will appreciate additional nozzle configurations useful and within the scope of the present invention.
While various materials and constructions of nozzles may be employed, machined or cast thermosetting polymeric materials such as cast epoxy or polyester resins or machined acrylic have been found suitable.
It should be understood that the invention is capable of a variety of modifications and variations which will become apparent to those skilled in the art upon reading of the specification. Such modifications are intended to be encompassed within the scope of the invention as defined by the appended claims. For instance, while the description and drawings depict a stationary discharge means and a moving electrode substrate, clearly the reverse roles could be taken and still maintain the desired relative movement.
What is claimed is:
l. A substantially closed loop system for pumping and metering viscous thixotropic electrochemically active paste through a discharge means comprising:
a. inlet means for charging make-up paste to said closed loop system;
b. first pump means for agitating and circulating said paste around the loop;
c. second pump means, downstream of said first pump means, for initiating flow of a portion of the circulating paste away from the closed loop to the discharge means; said second pump means metering a predetermined volumetric flow rate of paste to said discharge means.
2. The system of claim 1 wherein the flow rate of the discharged paste is virtually independent of the internal pressure of the paste exerted within the closed loop.
3. The system of claim I wherein said inlet means comprises a reservoir, battery paste within the reservoir, and biasing means applying a net positive suction head urging said battery paste to enter said closed loop.
4. The system of claim 1 wherein said paste has the characteristics of a non-Newtonian fluid comprising a major proportion of discrete finely divided crystalline particles slurried in a minor proportion of vehicle.
5. The system of claim 4 wherein said finely divided particles comprise oxides of lead.
6. The system of claim 5 wherein said vehicle com prises aqueous medium.
7. The system of claim 1 wherein said first pump means is located downstream from said inlet means and is a pump of the positive displacement type.
8. The system of claim 7 wherein said first pump means is a positive displacement pump of the archimedes screw type.
9. The system of claim 1 wherein said second pump means is a positive displacement pump of the archimedes screw type containing a metering valve.
10. The system of claim 1 wherein the ratio of the amount of paste allowed to recirculate in the closed loop to the amount of paste metered to said discharge means is from about 50:1 to about :1.
11. The system of claim 1 wherein said discharge means comprises a nozzle which converts a substantially cylindrical input flow from said second pump means to a substantially rectangular output flow for uniform delivery to a moving substrate.
12. The system of claim 11 wherein the internal fluid flow surfaces of said nozzle are substantially straight sided and further characterized by defining a passageway having an increasing cross-section from input to output as measured transverse to the direction of fluid flow.
13. The system of claim ll wherein the internal fluid flow surfaces of said nozzle define a passageway which is substantially conical as viewed perpendicularly to the direction of fluid flow and the length of the rectangular output.
14. The system of claim 13 wherein the passageway of the nozzle is characterized by a substantially constant cross-section from input to output as measured transverse to the direction of fluid flow.
15. A system including a substantially closed circulation loop for handling battery paste and metering it to a moving substrate in the production of battery electrode plates of the lead-acid type, comprising:
a source of highly viscous non-plastic thixotropic battery paste comprising a major proportion of oxides of lead suspended in a minor proportion of aqueous vehicle;
inlet means for charging make-up thixotropic paste to said closed loop system;
first pump means for agitating and circulating said paste around the loop;
discharge means positioned adjacent the substate for applying said paste to the substrate;
second pump means in connection with said discharge means, downstream of said first pump means, for initiating flow of a portion of the circulating paste away from the closed loop to the dis charge means;
said second pump means metering a predetermined volumetric flow rate of paste to said discharge means which is in turn metered to the substrate at the predetermined volumetric flow rate.
16. The system of claim 15 wherein said second pump means is a positive displacement pump of the progressing cavity type.
17. The system of claim 15 wherein the ratio of the amount of paste allowed to recirculate in the closed loop to the amount of paste metered to said discharge means is from about 50:1 to about 15: l.
18. The system of claim 15 wherein said discharge means comprises a nozzle which converts a substantially cylindrical input flow from said second pump means to a substantially rectangular output flow for uniform delivery to the substrate.
19. The system of claim 18 wherein the internal fluid flow surfaces of said nozzle define a passageway having an increasing cross-sectional area from input to output as measured transverse to the direction of paste flow.
20. The system of claim 18 wherein the internal fluid flow surfaces of said nozzle define a passageway which is substantially curved outwardly from input to output as viewed perpendicularly to the direction of paste flow and the length of the rectangular output.
21. The system of claim 18 wherein the passageway of the nozzle is characterized by a substantially constant cross-sectional area from input to output as measured transverse to the direction of paste flow.
22. The system of claim 18 wherein the outlet portion is substantially parallel to the surface formed by the substrate onto which the paste is to be deposited.

Claims (22)

1. A substantially closed loop system for pumping and metering viscous thixotropic electrochemically active paste through a discharge means comprising: a. inlet means for charging make-up paste to said closed loop system; b. first pump means for agitating and circulating said paste around the loop; c. second pump means, downstream of said first pump means, for initiating flow of a portion of the circulating paste away from the closed loop to the discharge means; said second pump means metering a predetermined volumetric flow rate of paste to said discharge means.
2. The system of claim 1 whErein the flow rate of the discharged paste is virtually independent of the internal pressure of the paste exerted within the closed loop.
3. The system of claim 1 wherein said inlet means comprises a reservoir, battery paste within the reservoir, and biasing means applying a net positive suction head urging said battery paste to enter said closed loop.
4. The system of claim 1 wherein said paste has the characteristics of a non-Newtonian fluid comprising a major proportion of discrete finely divided crystalline particles slurried in a minor proportion of vehicle.
5. The system of claim 4 wherein said finely divided particles comprise oxides of lead.
6. The system of claim 5 wherein said vehicle comprises aqueous medium.
7. The system of claim 1 wherein said first pump means is located downstream from said inlet means and is a pump of the positive displacement type.
8. The system of claim 7 wherein said first pump means is a positive displacement pump of the archimedes'' screw type.
9. The system of claim 1 wherein said second pump means is a positive displacement pump of the archimedes'' screw type containing a metering valve.
10. The system of claim 1 wherein the ratio of the amount of paste allowed to recirculate in the closed loop to the amount of paste metered to said discharge means is from about 50:1 to about 15:1.
11. The system of claim 1 wherein said discharge means comprises a nozzle which converts a substantially cylindrical input flow from said second pump means to a substantially rectangular output flow for uniform delivery to a moving substrate.
12. The system of claim 11 wherein the internal fluid flow surfaces of said nozzle are substantially straight sided and further characterized by defining a passageway having an increasing cross-section from input to output as measured transverse to the direction of fluid flow.
13. The system of claim 11 wherein the internal fluid flow surfaces of said nozzle define a passageway which is substantially conical as viewed perpendicularly to the direction of fluid flow and the length of the rectangular output.
14. The system of claim 13 wherein the passageway of the nozzle is characterized by a substantially constant cross-section from input to output as measured transverse to the direction of fluid flow.
15. A system including a substantially closed circulation loop for handling battery paste and metering it to a moving substrate in the production of battery electrode plates of the lead-acid type, comprising: a source of highly viscous non-plastic thixotropic battery paste comprising a major proportion of oxides of lead suspended in a minor proportion of aqueous vehicle; inlet means for charging make-up thixotropic paste to said closed loop system; first pump means for agitating and circulating said paste around the loop; discharge means positioned adjacent the substate for applying said paste to the substrate; second pump means in connection with said discharge means, downstream of said first pump means, for initiating flow of a portion of the circulating paste away from the closed loop to the discharge means; said second pump means metering a predetermined volumetric flow rate of paste to said discharge means which is in turn metered to the substrate at the predetermined volumetric flow rate.
16. The system of claim 15 wherein said second pump means is a positive displacement pump of the progressing cavity type.
17. The system of claim 15 wherein the ratio of the amount of paste allowed to recirculate in the closed loop to the amount of paste metered to said discharge means is from about 50:1 to about 15:1.
18. The system of claim 15 wherein said discharge means comprises a nozzle which converts a substantially cylindrical input flow from said second pump means to a substantially rectangular output flow for uniform delivery to the substrate.
19. The system of claim 18 wherein the internal fluid flow suRfaces of said nozzle define a passageway having an increasing cross-sectional area from input to output as measured transverse to the direction of paste flow.
20. The system of claim 18 wherein the internal fluid flow surfaces of said nozzle define a passageway which is substantially curved outwardly from input to output as viewed perpendicularly to the direction of paste flow and the length of the rectangular output.
21. The system of claim 18 wherein the passageway of the nozzle is characterized by a substantially constant cross-sectional area from input to output as measured transverse to the direction of paste flow.
22. The system of claim 18 wherein the outlet portion is substantially parallel to the surface formed by the substrate onto which the paste is to be deposited.
US421304A 1972-04-17 1973-12-03 Battery paste pumping and metering system Expired - Lifetime US3881654A (en)

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US4318430A (en) * 1979-11-07 1982-03-09 General Electric Company Apparatus for making rechargeable electrodes for electrochemical cells
EP0638945A1 (en) * 1993-08-11 1995-02-15 Gnb Battery Technologies Inc. Methods and apparatus for pasting battery current collectors
US6039545A (en) * 1998-03-31 2000-03-21 Mahr Corporation Method and apparatus for precision metering of high viscosity materials
US6340033B2 (en) * 1999-03-15 2002-01-22 Alcan International Limited Transfer of shear-thinning slurries
US6623673B1 (en) * 1999-09-03 2003-09-23 Datron-Electronic Gmbh Method for the metered discharge of a string of a viscous medium and feedpump for discharging a string of a viscous medium
US6969015B1 (en) * 2003-06-17 2005-11-29 Automatic Bar Controls Inc. Particulate sauce dispensing nozzle
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US20100097881A1 (en) * 2008-10-16 2010-04-22 Automatic Bar Controls Apparatus and Method for Mixing and Distributing a Food Product
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US20100097881A1 (en) * 2008-10-16 2010-04-22 Automatic Bar Controls Apparatus and Method for Mixing and Distributing a Food Product
US20100095887A1 (en) * 2008-10-16 2010-04-22 Automatic Bar Controls, Inc. Electronic Systems and Methods for Distributing a Food Product Over a Turntable
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