US2551360A - Art of subjecting effervescent materials to an electric field - Google Patents

Art of subjecting effervescent materials to an electric field Download PDF

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US2551360A
US2551360A US644616A US64461646A US2551360A US 2551360 A US2551360 A US 2551360A US 644616 A US644616 A US 644616A US 64461646 A US64461646 A US 64461646A US 2551360 A US2551360 A US 2551360A
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receptacle
subjecting
liquid
electric field
electrodes
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Rudolph A Bierwirth
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RCA Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C41/00Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/02Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C41/04Rotational or centrifugal casting, i.e. coating the inside of a mould by rotating the mould
    • 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
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S159/00Concentrating evaporators
    • Y10S159/11Biologicals
    • 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
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S159/00Concentrating evaporators
    • Y10S159/16Vacuum
    • 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
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S159/00Concentrating evaporators
    • Y10S159/26Electric field

Definitions

  • This invention relates to improvements in the art of subjecting effervescent or ebullient liquids to an electric field and, though not necessarily limited thereto, will be described as applied to the concentration by evaporation or distillation of pharmaceutical and biological liquids.
  • Brown system for treating effervescent liquids with an electric iield is capable of handling bulk quantities of such liquids
  • the quantity which can be treated is nevertheless limited, as in the Bierwirth system, to a predetermined charge. That is to say, neither the Brown system nor the Bierwirth system is capable of handling a continuous flow of material.
  • the principal object of the present invention is to provide a simple and reliable method of subjecting a movingstream or column of liquid to the action of an electric iield, and one which may be applied to the treatment of liquids which eiervesce or which are unstable or labile when subjected to such a field by anyY ordinary method.
  • Another and important object of the present invention is to provide an electronic centrifuge which may be operated continuously at subatmospheric pressuresy without danger of ionizing the ambient or causing an arc-over between the field4 electrodes or other parts of the centrifuge.
  • a related object of the present invention is to provide an electronic dehydration apparatus which shall be capable of concentrating any desired quantity of liquid, including liquids that are unstable or labile at ordinary temperatures. and one which, by reason of the simplicity and compactness of its parts, may be incorporated within a bell jar or other vacuum chamber of conventional form and dimensions.
  • Fig. l is s, partly diagrammatic sectional elevation of an electronic centrifuge constructed in accordance with the principle of the invention
  • Fig. 2 is a top plan view of the device of Fig. 1,
  • FIG. 3 is an enlarged elevational View of the rotatable receptacle of Fig. 1, showing the arrangement of the electrodes thereon and,
  • Fig. 4 is an electrical diagram which will be referred to in explaining the oper-ation of the device.
  • I designates an inverted transparent bell jar which is closed at its opposite ends by Vacuumtight lids or closure elements 2 and 3, respectively.
  • the space d within the jar or chamber I is evacuated through a port 5 in the lid 2 by means of a suitable vacuum pump, not shown, but which will be understood to be connected to the said port through a water cooled condenser 6 and pipe l.
  • a rotatable spindle or shaft ⁇ 8 extends into the evacuable space :i through a vacuumtight bearing ⁇ El at the center of the lid 2.
  • This shaft 8 is provided on its outer end with driving wheel IE) which may be driven by a suitable gear or belt, not shown, and has an inverted cylindrical or cup-shape receptacle I I aflixed to its inner end as by means of a set screw I2.
  • Ihe receptacle I I is necessarily constituted of an insulating material, and is preferably formed of polyethylene or other suitable material.
  • Two spaced apart electrodes in the form of metal bands or rings I3 and I4 are mounted preferably one above the other, in capacitive relation, on the outer surface of the rotatable receptacle I l. As shown in both Figs. 1 and 3 the electrodes I3 and I4 may be seated in grooves in the cylndrical wall of the receptacle and secured therein as by means of insulating straps I5 and I6, respectively.
  • the energy required to establish an electric or electrostatic field within the rotatable receptacle li is applied to the capacitor electrodes i3 and by means of an electrically secondary coil If which is mounted on the outer surface of the said receptacle preferably in the space between the said electrodes.
  • the secondary coil il in turn receives its energy from a radio frequency oscillator i9 through two leads i9 and which terminate within the evacuable space 4 in a primary coil 2i which extends in spaced relation around the secondary coil i'l.
  • This rotatable secondary coil i7 is thus inductively coupled to the stationary primary coil 2l.
  • the penicillin liquor, or other iiuent material, is entered into the rotating receptacle il from a reservoir 22 through a pipe or tube 23 which terminates in a restricted opening 23a adjacent to the closed or upper end of the said receptacle.
  • a suitable valve 2li in the tube 23 is employed for regulating the flow of the liquid which is drawn from the reservoir 22 into the receptacle i! by reason of the partial vacuum which is created within the evacuable space l in which the said receptacle rotates.
  • the liquid to be processed enters the electried column (i. e. the space within the rapidly rotation receptacle l i) adjacent to the top of the said column, it may be said to be subjected to gravitation as well as to centrifugal force.
  • the drug liquor or other fluent material enters the rapidly rotating receptacle a' i from the nozzle 23a it will be spread in the form of a liquid lm over the inner surface of the said receptacle and, as the depth of the liquid (on the inner side walls) increases, will flow gradually downwardly, through th-e electric eld and over the inwardly turned rim lia, from whence it drops onto the lower plate or base 3 ci the bell jar l.
  • An outlet pipe 25 in the base 3 conducts the now concentrated liquid to a storage container 25 outside of the vacuum chamber'.
  • This pipe 25 is provided with a stop cock or similar valve 2 having two passageways Zia and 2lb therein, which serve,
  • the oscillator i8 be tuned to the frequency, or approximate frequency, of the utilization circuit.
  • the utilization circuit comprises the secondary coil i'i and, in effect, two capacitors C and C', with the liquid (which is a dielectric and represented by the symbol Z) in series between the said capacitors.
  • the liquid which is a dielectric and represented by the symbol Z
  • the invention is obviously not limited to the use of an oscillator of a particular frequency and power, nor to the use of a rotating receptacle of specific dimensions, it may well be set forth, by way of example, the details of construction and operation of'a specific successful embodiment of the invention.
  • the apparatus was designed to effect a reduction of ve-to-one, within one hour, of ten liters of penicillin liquor (or other semi-conducting liquid).
  • the electrical energy employed in heating the liquid was supplied by a two kilowatt oscillator operating at a frequency of 30 megacycles per second and the vacuum pump was adjusted to maintain a vacuum in the main chamber of the order of from 20 to 30 millimeters of mercury when the receptacle i l was rotated at a speed of about 900 RPJM.
  • the centrifugal force to Iwhich the liquid material Iwas subjected when rotated at this speed was estimated to be about 30x gravity.
  • the electrodes I3 and i4 comprised 1% inch copper bands spaced .apart about 21/4 inches.
  • rlhe Secondary coil (Il) comprised two turns of numb-er 10 gauge copper wire, spaced Tse inch between centers and the primary coil 2i comprised but a single turn of copper tubing spaced about l/2 inch from the secondary coil.
  • the present invention provides a simple and reliable continuous flow method of and apparatus for subjecting ebullient liquids to an electric eld.
  • Apparatus for the treatment of materials comprising, a rotatable receptacle for the material to be treated, a plurality of ring-like electrodes in the form of metal bands mounted in spaced capacitive relation on the sides of said receptacle for generating an electric field within said receptacle, a transformer comprising a secondary coil mounted on said rotatable receptacle and connected to said electrodes and a stationary primary coil mounted adjacent to said rotatable receptacle in spaced inductive relation with respect to said secondary coil.

Description

BIERWIRTH AN ELECTRI C FIELD llll/ INVENToR @0.004 Pff A. /f/ew/er/f ATTORNEY Filed Jan. 31, '1946 ART OF SUBJECTING EFFERVESCENT MATERIALS TO May 1, 1951 lefasc,
ffy. 4,
Patented May 1, 1951 ART OF SUBJECTING EFFERVESCENT MATERIALS T AN ELECTRIC FIELD Rudolph A. Bierwirth, Brinceton, N. J., assigner to Radio Corporation of America, a corporation of Delaware Application January 3l, 1946, Serial No. 644,616
(Cl. 21B-47) 2 Claims.
This invention relates to improvements in the art of subjecting effervescent or ebullient liquids to an electric field and, though not necessarily limited thereto, will be described as applied to the concentration by evaporation or distillation of pharmaceutical and biological liquids. v
It has previously been demonstrated (see copending application of Rudolph A. Bierwirth, lSer. No. 557,053) that various effervescent liquids such, for example, as penicillin liquor, may be dehydrated,` in dosage quantities, by mounting the ampoules in which the liquid is contained between a pair of spaced apart electrodes and rotating them about their vertical axes at a speed calculated to cause the liquid to be spread, by centrifugal force, over the inner side walls of the ampoules. Bierwirths method yand apparatus not only prevent the generation of bubbles (which might be carried away with the vapor) but also speeds up the dehydration process. This is so because the liquid, when subjected to centrifugal force, presents a greatly enlarged surface area to the electric eld between the spaced apart electrodes.
If an effort is made to increase the output of Bierwirths apparatus by the use of a larger receptacle and more powerful electrical and mechanical forces it becomes increasingly difhcult and eventually impossible to maintain satisfactory operating parameters such, for example, as an adequate coefficient-of coupling between the electric eld and the rapidly rotating liquid. This is especially so when the material being processed is subject to subatmospheric pressure since, in that case, if the electrical power is increased to compensate for the increased quantity of material being treated the danger of ionizing the ambient and establishing an arc-over is likewise increased.
Up to now the only electric field method of treating large quantities of eiervescent liquids has involved the use of stationary electrodes, which are usually clamped to the outer surface o the receptacle, and an auxiliari7 save-all system mounted within or adjacent to the receptacle for breaking-up (rather than preventing the generation of) bubbles and foam. Such a bulk reducing save-all system is described in copending application of George H. Brown et al., Ser. No. 536,491, now abandoned.
While the Brown system for treating effervescent liquids with an electric iield is capable of handling bulk quantities of such liquids, the quantity which can be treated is nevertheless limited, as in the Bierwirth system, to a predetermined charge. That is to say, neither the Brown system nor the Bierwirth system is capable of handling a continuous flow of material.
Accordingly, the principal object of the present invention is to provide a simple and reliable method of subjecting a movingstream or column of liquid to the action of an electric iield, and one which may be applied to the treatment of liquids which eiervesce or which are unstable or labile when subjected to such a field by anyY ordinary method.
Another and important object of the present invention is to provide an electronic centrifuge which may be operated continuously at subatmospheric pressuresy without danger of ionizing the ambient or causing an arc-over between the field4 electrodes or other parts of the centrifuge.
A related object of the present invention is to provide an electronic dehydration apparatus which shall be capable of concentrating any desired quantity of liquid, including liquids that are unstable or labile at ordinary temperatures. and one which, by reason of the simplicity and compactness of its parts, may be incorporated within a bell jar or other vacuum chamber of conventional form and dimensions.
The invention will be described in connection with the accompanying drawing wherein:
Fig. l is s, partly diagrammatic sectional elevation of an electronic centrifuge constructed in accordance with the principle of the invention,
Fig. 2 is a top plan view of the device of Fig. 1,
3 is an enlarged elevational View of the rotatable receptacle of Fig. 1, showing the arrangement of the electrodes thereon and,
Fig. 4 is an electrical diagram which will be referred to in explaining the oper-ation of the device.
In the illustrated embodiment of the invention I designates an inverted transparent bell jar which is closed at its opposite ends by Vacuumtight lids or closure elements 2 and 3, respectively. The space d within the jar or chamber I is evacuated through a port 5 in the lid 2 by means of a suitable vacuum pump, not shown, but which will be understood to be connected to the said port through a water cooled condenser 6 and pipe l. A rotatable spindle or shaft `8 extends into the evacuable space :i through a vacuumtight bearing `El at the center of the lid 2. This shaft 8 is provided on its outer end with driving wheel IE) which may be driven by a suitable gear or belt, not shown, and has an inverted cylindrical or cup-shape receptacle I I aflixed to its inner end as by means of a set screw I2. Ihe receptacle I I is necessarily constituted of an insulating material, and is preferably formed of polyethylene or other suitable material.
Two spaced apart electrodes in the form of metal bands or rings I3 and I4 are mounted preferably one above the other, in capacitive relation, on the outer surface of the rotatable receptacle I l. As shown in both Figs. 1 and 3 the electrodes I3 and I4 may be seated in grooves in the cylndrical wall of the receptacle and secured therein as by means of insulating straps I5 and I6, respectively.
The energy required to establish an electric or electrostatic field within the rotatable receptacle li is applied to the capacitor electrodes i3 and by means of an electrically secondary coil If which is mounted on the outer surface of the said receptacle preferably in the space between the said electrodes. The coil il here illus trated 'comprises but two turns of wire and has its opposite ends soldered, or otherwise conductively affixed, one to one electrode i3 and the other to the other electrode Ecl. The secondary coil il in turn receives its energy from a radio frequency oscillator i9 through two leads i9 and which terminate within the evacuable space 4 in a primary coil 2i which extends in spaced relation around the secondary coil i'l. This rotatable secondary coil i7 is thus inductively coupled to the stationary primary coil 2l.
The penicillin liquor, or other iiuent material, is entered into the rotating receptacle il from a reservoir 22 through a pipe or tube 23 which terminates in a restricted opening 23a adjacent to the closed or upper end of the said receptacle. A suitable valve 2li in the tube 23 is employed for regulating the flow of the liquid which is drawn from the reservoir 22 into the receptacle i! by reason of the partial vacuum which is created within the evacuable space l in which the said receptacle rotates.
Since the liquid to be processed enters the electried column (i. e. the space within the rapidly rotation receptacle l i) adjacent to the top of the said column, it may be said to be subjected to gravitation as well as to centrifugal force. Thus, as the drug liquor or other fluent material enters the rapidly rotating receptacle a' i from the nozzle 23a it will be spread in the form of a liquid lm over the inner surface of the said receptacle and, as the depth of the liquid (on the inner side walls) increases, will flow gradually downwardly, through th-e electric eld and over the inwardly turned rim lia, from whence it drops onto the lower plate or base 3 ci the bell jar l. An outlet pipe 25 in the base 3 conducts the now concentrated liquid to a storage container 25 outside of the vacuum chamber'. This pipe 25 is provided with a stop cock or similar valve 2 having two passageways Zia and 2lb therein, which serve,
selectively, (a) to pass the liquid into the container and (b) to admit air in the chamber 4 when the dehydration process has been completed.
In reducing the invention to practice it is imi portant that the oscillator i8 be tuned to the frequency, or approximate frequency, of the utilization circuit. As indicated in Fig. 4 the utilization circuit comprises the secondary coil i'i and, in effect, two capacitors C and C', with the liquid (which is a dielectric and represented by the symbol Z) in series between the said capacitors. Since industrial oscillators are usually designed to operate most efficiently at a particular fre quency (rather than over a wide band of fre quencies) it is usually necessary to design the cup-shape receptacle i! and its associated electrical fixtures with a careful regard to the frequencyvof the oscillator and also with regard to the desired capacity (in liters per hour) of the system. Thus, while the invention is obviously not limited to the use of an oscillator of a particular frequency and power, nor to the use of a rotating receptacle of specific dimensions, it may well be set forth, by way of example, the details of construction and operation of'a specific successful embodiment of the invention. In one such embodiment the apparatus was designed to effect a reduction of ve-to-one, within one hour, of ten liters of penicillin liquor (or other semi-conducting liquid). In this case the electrical energy employed in heating the liquid was supplied by a two kilowatt oscillator operating at a frequency of 30 megacycles per second and the vacuum pump was adjusted to maintain a vacuum in the main chamber of the order of from 20 to 30 millimeters of mercury when the receptacle i l was rotated at a speed of about 900 RPJM. The centrifugal force to Iwhich the liquid material Iwas subjected when rotated at this speed was estimated to be about 30x gravity. The dimensions of the polyethylene receptacle il were approximately as follows: thickness of Walls: 0.25 of an inch; depth=6 inches; inside diameter :4l/2 inches; inside diameter of the rim (Ila) 37/8 inches. The electrodes I3 and i4 comprised 1% inch copper bands spaced .apart about 21/4 inches. rlhe Secondary coil (Il) comprised two turns of numb-er 10 gauge copper wire, spaced Tse inch between centers and the primary coil 2i comprised but a single turn of copper tubing spaced about l/2 inch from the secondary coil.
'it ywill now be apparent that the present invention provides a simple and reliable continuous flow method of and apparatus for subjecting ebullient liquids to an electric eld.
What is claimed is:
1. Apparatus for the treatment of materials comprising, a rotatable receptacle for the material to be treated, a plurality of ring-like electrodes in the form of metal bands mounted in spaced capacitive relation on the sides of said receptacle for generating an electric field Within said receptacle, a transformer comprising a secondary coil mounted on said rotatable receptacle and connected to said electrodes and a stationary primary coil mounted adjacent to said rotatable receptacle in spaced inductive relation with respect to said secondary coil.
2. The invention as set forth in claim 1 and wherein said secondary coil is mounted in the space between said electrodes on said rotatable receptacle and said stationary primary coil is mounted in register with said secondary coil.
RUDOLPH A. BIERWIRTH.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 548,150 Williams et al Oct. 15, 1895 1,405,085 Zahm Jan. 31, 1922 1,415,255 Miller May 9, 1922 1,530,140 Schneible Mar. 17, 1925 i,900,573 McArthur Mar. 7, 1933 2,109,323 Smith Feb. 22, 1938 2,167,718 Harris, Jr., et al. Aug. 1, 1939 2,261,847 Dufour' et al. Nov. 4, 1941 2,280,851 Soin-es Apr. 28, 1942 2,351,300 Somes June 13, 1944 2,459,622 Cohoe et al Jan. 18, 1949 2,459,623 Cohoe et al. Jan. 18, 1949
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2865445A (en) * 1954-10-14 1958-12-23 Buchler Joseph Evaporator
US2884050A (en) * 1954-03-23 1959-04-28 Lloyd E Brownell Centrifugal evaporator
US3204687A (en) * 1963-07-23 1965-09-07 Ralph G Sargeant Centrifugal electrical apparatus for treating liquids
US3209812A (en) * 1959-09-22 1965-10-05 Ralph G Sargeant Apparatus for removing water from liquid mixtures
US3377417A (en) * 1965-04-30 1968-04-09 Emil R. Capita Centrifugal furnace

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US548150A (en) * 1895-10-15 phillips
US1405085A (en) * 1919-09-12 1922-01-31 Zahm & Nagel Co Inc Process and apparatus for concentrating liquids
US1415255A (en) * 1918-05-10 1922-05-09 Evaporating And Drying Machine Evaporator
US1530140A (en) * 1921-04-16 1925-03-17 Claude D Schneible Evaporator
US1900573A (en) * 1930-11-19 1933-03-07 Gen Electric Electric heating apparatus
US2109323A (en) * 1937-07-08 1938-02-22 Compo Shoe Machinery Corp Shoe cementing apparatus
US2167718A (en) * 1935-12-26 1939-08-01 Standard Oil Dev Co Apparatus for subjecting liquids to silent electric discharge
US2261847A (en) * 1935-10-29 1941-11-04 Dufour Rene Method for heating and vulcanizing rubber and similar matter
US2280861A (en) * 1936-08-20 1942-04-28 Budd Induction Heating Inc Transformer distributing system
US2351300A (en) * 1942-05-25 1944-06-13 Budd Induction Heating Inc Induction heating apparatus
US2459622A (en) * 1944-03-18 1949-01-18 Fred K H Levey Co Inc Method of and apparatus for drying sheet materials by high-frequency electric fields
US2459623A (en) * 1945-05-05 1949-01-18 Fred K H Levey Co Inc Method and apparatus for drying sheet materials

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US548150A (en) * 1895-10-15 phillips
US1415255A (en) * 1918-05-10 1922-05-09 Evaporating And Drying Machine Evaporator
US1405085A (en) * 1919-09-12 1922-01-31 Zahm & Nagel Co Inc Process and apparatus for concentrating liquids
US1530140A (en) * 1921-04-16 1925-03-17 Claude D Schneible Evaporator
US1900573A (en) * 1930-11-19 1933-03-07 Gen Electric Electric heating apparatus
US2261847A (en) * 1935-10-29 1941-11-04 Dufour Rene Method for heating and vulcanizing rubber and similar matter
US2167718A (en) * 1935-12-26 1939-08-01 Standard Oil Dev Co Apparatus for subjecting liquids to silent electric discharge
US2280861A (en) * 1936-08-20 1942-04-28 Budd Induction Heating Inc Transformer distributing system
US2109323A (en) * 1937-07-08 1938-02-22 Compo Shoe Machinery Corp Shoe cementing apparatus
US2351300A (en) * 1942-05-25 1944-06-13 Budd Induction Heating Inc Induction heating apparatus
US2459622A (en) * 1944-03-18 1949-01-18 Fred K H Levey Co Inc Method of and apparatus for drying sheet materials by high-frequency electric fields
US2459623A (en) * 1945-05-05 1949-01-18 Fred K H Levey Co Inc Method and apparatus for drying sheet materials

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2884050A (en) * 1954-03-23 1959-04-28 Lloyd E Brownell Centrifugal evaporator
US2865445A (en) * 1954-10-14 1958-12-23 Buchler Joseph Evaporator
US3209812A (en) * 1959-09-22 1965-10-05 Ralph G Sargeant Apparatus for removing water from liquid mixtures
US3204687A (en) * 1963-07-23 1965-09-07 Ralph G Sargeant Centrifugal electrical apparatus for treating liquids
US3377417A (en) * 1965-04-30 1968-04-09 Emil R. Capita Centrifugal furnace

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