Treatment of fluids

Information

  • Patent Grant
  • 6913382
  • Patent Number
    6,913,382
  • Date Filed
    Friday, April 27, 2001
    23 years ago
  • Date Issued
    Tuesday, July 5, 2005
    18 years ago
Abstract
A method for fixing a first fluid within a second fluid which includes the steps of mixing the first and second fluids together and subjecting the first and second fluids to an electric field and a high voltage corona like electric discharge. The method can be used, for example, to increase the oxygen content of water. It can also be used for the treatment of waste effluent. An apparatus for carrying out the process includes a fluid passageway defined between inner and outer elongated conduits with a preferably spirally configurated baffle means in the passageway and a plurality of electrode needles extending into the passageway.
Description

The present invention relates to the treatment of fluids and more particularly, relates to devices and methods for the treatment of fluids to change the properties thereof.


The treatment of a fluid with either a magnetic field or an electric field is well known in the art. For example, it is known to treat water to reduce problems associated with scaling and corrosion of the equipment using the water. In particular, the use of high temperature water in boilers and the like has caused significant problems and there have been proposals in the art for treating the water in order to reduce problems of scaling and corrosion.


It is also known in the art to use electrostatic fields to treat the water such that particles in suspension become charged and can be attracted and/or repelled as desired. This principle is also used in processes such as paint spraying and photocopiers.


While the use of electrostatic fields has been known in the art, there has been minimal acceptance of the use of such devices. Furthermore, the use of such devices has been limited to very specific situations.


Thus, German Patent 197 17 495 A1 teaches the use of an electric discharge with a plasma effect on fluids in the presence of gas generated by the corona effect.


German Patent 198 30 956 A1 teaches a method using electrical pulsation to kill biological pollutants.


U.S. Pat. No. 4,175,871 teaches a fluid mixing apparatus having means for producing vortex like motions of the fluids; the patentee teaches generation of electric fields producing an enhanced overall mixing process.


U.S. Pat. No. 5,235,905 teaches a method to create a preservation effect on perishable foods by using a pulse electrical arc in a pressurized environment.


U.S. Pat. No. 4,085,170 teaches a method for dispersing homogeneously the gas in a liquid using electrical discharge which increases a surface contact of the gas in a liquid by breaking the gas bubbles into micro bubbles.


U.S. Pat. No. 5,766,447 teaches a method of killing microorganisms in an aqueous solution using AC energy with pulsation.


WO 94/16809 teaches the use of a high voltage electrical current pulsator to purify a liquid by discharging a pulsation between two electrodes creating a plasma and forming a shock wave.


WO 99/47230 teaches a high voltage pulsation creating an acoustic shock wave and generating a plasmic reaction.


It is an object of the present invention to provide an apparatus which may be used to treat fluids with an electrostatic discharge.


It is a further object of the present invention to provide a method for the treatment of a fluid to change the characteristics of the fluid.


It is a further object of the present invention to provide a method for the fixation of a first fluid within a second fluid.


It is a further object of the present invention to provide a method for the fixation of a gas within a different fluid.


It is a further object of the present invention to provide a method for reducing the contamination of a fluid.


It is a particular object of the present invention to provide a method for a fixation of oxygen in water.


According to the present invention, in a method for fixing a first fluid in a second fluid comprising the steps of mixing the first and second fluids together, there is the improvement which comprises the step of passing the fluid between two electrodes, a first one of the electrodes being formed of a metallic material having a dielectric covering thereon, a second one of the electrodes being formed of a metallic material and being grounded, and applying a DC voltage to the first of the electrodes.


In a further aspect of the present invention, in an apparatus for fixing a first fluid in a second fluid wherein the apparatus has an outer elongated conduit, an inner coaxial conduit, the inner coaxial conduit being of a metallic material and having a dielectric material coated thereon, a fluid passageway defined intermediate the outer elongated conduit and inner coaxial conduit, means for introducing a first and second fluid into the fluid passageway, spirally arranged baffle means within the fluid passageway to cause fluids passing therethrough to circulate in a spiral configuration, a plurality of electrode needles in electrical communication with the outer conduit and extending inwardly towards the inner coaxial conduit, the improvement comprising a conical section formed between opposed ends of the inner and outer conduits, the conical section having a decreasing cross sectional area in the direction of fluid flow, and means for applying a DC voltage to the inner conduit, the baffle means being electrically grounded.


In a preferred embodiment, the baffle means are mounted within the fluids passageway to cause a fluid introduced at a first end of the passageway to circulate in a spiral configuration therein. A particularly preferred arrangement comprises one wherein a spiral member is used wherein the inwardly extending edge of the spiral member has a tapered sharp configuration. Even more preferably, there are provided a plurality of electrode needles which can cause a corona like discharge.


Preferably, the system of the present invention is designed to be operated at a voltage of at least 10 kV.


The ability of a liquid to hold soluble a gas is finite and is a function of both pressure and temperature. One everyday example of utilizing a pressure to maintain a gas soluble is that of soda drinks wherein they are carbonated and maintained under pressure to maintain the gas soluble within the liquid. Once the cap is removed and pressure is released, the solubility of the gas decreases and over time, the drink will go flat.


According to one method of the present invention, when a gas is introduced to a liquid, both being under pressurization, and the liquid and dissolved gas are passed through an electric field having a voltage of at least ±10 kV, the gas will remain “dissolved” in the liquid beyond the normal capacity of the liquid to hold such a gas. Preferably, the voltage will be ±15 kV.


The mechanism for the ability of the gas to remain within the liquid is not fully understood. Thus, while applicant will use the term “dissolve”, it is well understood that a different mechanism other than the standard definition of solution may be employed. For purposes of this application, applicant will use the terms “fix” or “fixation” as a description of the mechanism of retention of the gas within the liquid. However, applicant does not intend to be limited by this term; rather, it will be understood that any bonding mechanism or other means of retaining the gas within the liquid will fall within the scope of the invention when the method of the invention is practiced.


The method of the present invention can be applied with many different fluids. First of all, one can have a fixation of a gas within a liquid, a fixation of a first gas within another gas, or a fixation of a liquid within a second liquid. The scope of the present invention also includes the fixation of a liquid to a gas. Still further, the present invention can be practiced for the fixation of a liquid or a gas with certain types of solids, and particularly flowable solids.


The particular gas/liquid/solid will depend upon the particular end use desired. Some of the possibilities are discussed herein below.


A first method of the present invention would involve the fixation of a gas within a liquid. Many uses for such a method can be envisaged including, for example, the fixation of oxygen within water. The use of such a material can range widely from medicinal use to the treatment of cyanide containing water such as is encountered in many mining operations. Other potential uses would include, for example, a nitrogen gas within a liquid for use as a fertilizer. One suffices to say that wherever the use of a particular gas in conjunction with a liquid is desirable, the method of the present invention can be practiced within the limits dictated by normal practice—i.e. a question of the safety of the product involved including either the liquid or the gas.


A method of the present invention can also be utilized to treat food products for various purposes including the ability to enhance the storage of the products and/or the use of the invention as a bactericide. Thus, the present invention can be utilized as a cold pasteurization of products such as milk and/or juices and the like.


A further method of the present invention would involve the treatment of a flowable product such as a resin which has been used in a treatment system wherein the resin adsorbs/absorbs different chemicals on its surface. With the method of the present invention, one can pass the resin through the treatment of the present invention to renew the resin. Furthermore, one can use a gas to fixate the gas within the resin to enhance the efficacy thereof.


A unique feature of the present invention is the fact that the gas will remain “fixed” within the liquid for a substantial period of time. Referring to the case of oxygen within water, when get in a bottled condition, there is minimal loss of the properties—i.e. the oxygen remains fixed. When exposed to air ambient temperature, there is a loss, in one week, of between 5%-10% of the fixed oxygen. It is being found that freezing the water with the fixed oxygen causes a substantial loss of oxygen content. However, one can boil the water with fixed oxygen with some loss thereof. The oxygen content is preferably between 50 and 100 ppm although it can reach as much as 140 ppm.


A further aspect of the present invention comprises the treatment of a fluid to decontaminate the fluid. Examples of such fluids can range from waste products from industrial processes through to municipal sewage. It has been found that treatment of the waste material is highly effective in removing contaminates and in purifying the liquid.





Having thus generally described the invention, reference will be made to the accompanying drawings and examples showing embodiments thereof, in which:



FIG. 1 is a schematic illustration of a first system for the treatment of water with a gas such as oxygen for the bottling thereof;



FIG. 2 is a schematic illustration of a system for the fixation of a gas within a liquid;



FIG. 3 is a side elevational view of a spiral component for use in causing an electrical discharge within the water; and



FIGS. 4 to 10 are graphs illustrating the measurement of blood oxygen after intake of oxygenated water as set forth in Example 10.





Initially, it will be understood that the specific descriptions herein relating to the treatment of water or a liquid with a gas may equally well be applied to other materials as discussed hereinabove.


Turning to FIG. 1, there is shown a system for providing oxygen rich water which may be bottled. In this arrangement, there is provided a dosage pump 1 operatively associated with a reservoir 1A of water cooled to approximately 4° C. A pressure pump 2 is operatively connected to an outlet conduit which in turn leads to a membrane sparging diffuser having a control member 5 associated therewith. A mixer 6 is connected to a bottle of oxygen 7 and the gas and water will then pass through the induction system 8 of the present invention. Induction system 8 is provided with a high voltage power supply 9 and a special ground 10.


An oxygen controller 11 is provided as well as a conductivity controller 12. A jig or valve structure 13 is provided for controlling and maintaining the pressure of the oxygen within the water. Subsequently, the water will go through a bottling station 14. A control panel 15 provides suitable controls for the operation of the system.


Turning to FIG. 2, there is illustrated a second system for the fixation of a gas such as oxygen in a liquid such as water. In this arrangement, there is provided a suitable electric source 101 connected to a high power supply 102 capable of supplying electricity at a voltage of 50 kV DC or above. A suitable ground 103 is provided.


There is provided an induction device generally designated by reference numeral 104 and which includes, within the device, a conductor 105, a dielectric 106 in a Teflon material, a spiral 107 of a metallic material such as stainless steel, and an outer envelope 108. This is all encompassed in a first section 109 of the induction system. This is substantially as shown in PCT/CA/99/00274, the disclosure of which is hereby incorporated.


In a second section 114, there is provided a conductor 110 in a conical arrangement, a spirally wound dielectric 111 in a conic configuration and a spiral 112 in stainless steel. This is all contained in an outer package 114.


In a third section 120, there is again provided a conductor 115, a spirally wound dielectric 116, stainless 117 and an outer envelope or container 118. This is all contained in a package 120.


The arrangement includes a entry 122 for the conductor wires and a diffuser membrane 123. Reference numeral 124 indicates an ionization by a dielectric effect. There is provided a diffuser 125 to permit the entry of a gas into the water while there is provided a multiple point ionization arrangement 126 which provides a corona effect by a cycling system preferably at 50 kV or above and with a current of 5 MA or above.


Subsequently, there is provided a mixer 127.


As shown in FIG. 3, interiorly there is provided a member within the conduit for electrical discharge. As shown, there are a pair of side bar members 300 with a spirally wound member 303 having tapered edges extending inwardly to provide a sharp point generally designated by reference numeral 306.


At points along the spiral, there are provided discharge electrodes 308 which again are provided with a sharp point and are designed to discharge at intervals to provide a corona effect.


The following examples are illustrative of some of the different aspects of the present invention.


EXAMPLE 1

Municipal waste from an urban municipality were subjected to a treatment in an apparatus according to the present invention. The waste water was treated without using any gas, using air, oxygen, carbon dioxide and nitrogen. The results are given in Table 1, hereinbelow.
















Control
Treated














Parameters
Units
Not Treated
No gas
Air
O2
CO2
N2

















pH

7.15
7.29
7.34
7.41
5.39
6.40




±0.01
±0.07
±0.11
±0.04
±0.05
±0.07


POR
(mV)
112
89
111
141
179
124




±23
±28
±1
±4
±4
±9



(° C.)
19.8
19.8
20.5
20.6
20.9
21.1




±0.5
±0.1
±0.1
±0.2
±0.2
±0.4


DCOtot
(mg/L)
1670
1440
1790
1560
1460
1710




±120
±100
±400
±150
±190
±210


DCOsol
(mg/L)
113
115
80
95
120
80




±25
±35
±35
±10
±20
±15


MES
(mg/L)
113
117
169
187
182
177




±37
±15
±33
±26
±15
±40


MVS
(mg/L)
97
95
144
152
160
158




±42
±13
±43
±198
±15
±16


PO43−
(mg/L)
1.87
1.49
1.68
1.73
1.76
1.60




±0.06
±0.17
±0.01
±0.03
±0.01
±0.01


NH4+
(mg/L)
15.1
12.8
14.7
14.6
14.7
14.0




±0.6
±1.6
±0.1
±0.3
±0.8
±0.5





Explanation:


POR—Oxygen Potential Reduction


DCOtot—Chemical Oxygen Demand (Total)


tot—Total


DCOsol—Chemical Oxygen Demand (Solution)


sol—Solution


MES—Material in Suspension


MVS—Material in Suspension (Volatile)






From the above results, the treatment without a gas and with the addition of carbon dioxide permitted a reduction in the concentration of DCO sub-total without affecting the DCO sub-base.


EXAMPLE 2

The solid waste from a municipal plant was subjected to treatment with the apparatus of the present invention. The trials were carried out using the injection of air, oxygen, carbon dioxide and nitrogen. A trial was also run without the injection of a gas. The results are set forth in Table 2 hereinbelow.
















Control
Treated














Parameters
Units
Not Treated
No gas
Air
O2
CO2
N2

















pH

6.43
7.17
8.45
6.64
5.53
6.69




±0.04
±0.05
±0.01
±0.03
±0.02
±0.02


POR
(mV)
−124
436
499
59
67
−83




±9
±4
±15
±13
±7
±20



(° C.)
17.7
19.9
21.4
20.1
21.3
22.4




±0.2
±0.1
±0.1
±0.3
±0.3
±0.1


DCOtot
(mg/L)
14000
5510
5040
5230
5340
5810




±3110
±1040
±1040
±800
±720
±200


DCOsol
(mg/L)
349
599
1010
397
476
383




±20
±43
±60
±7
±6
±9


MES
(mg/L)
4860
4020
3280
3710
3570
3720




±30
±60
±100
±30
±50
±100


MVS
(mg/L)
3330
2690
2180
2610
2630
2670




±30
±40
±80
±30
±20
±70


PO43−
(mg/L)
1.59
3.55
5.77
2.66
2.27
2.92




±0.06
±0.17
±0.02
±0.21
±0.10
±0.35


NH4+
(mg/L)
47.0
41.3
11.3
54.4
52.2
54.8




±1.4
±2.3
±0.7
±2.7
±2.7
±1.8









March variations were noted in the POR both without injection of a gas and with injections of air. A substantial decrease in the DCO sub-total was measured with all treatments. This was accompanied by an increase in the DCO sub-base. The treatment with oxygen was interesting since it permitted a decrease of 62.6% of the DCO total while causing only a slight increase in the DCO base.


Interesting was the ability of the treatment to remove disagreeable odors. In particular, the treatment without a gas and with air substantially reduced the disagreeable odors while the remaining treatments also reduce the odors, but to a lesser degree.


EXAMPLE 3

Used water from a pulp was subjected to a treatment as set forth in Examples 1 and 2. The results are set forth in Table 3 hereinbelow.















Treated














Parameters
Units
Control Not Treated
No gas
Air
O2
CO2
N2

















pH

8.67
8.54
8.59
8.66
4.63
7.92




±0.02
±0.01
±0.01
±0.01
±0.03
±0.01


POR
(mV)
3
5
23
47
200
65




±25
±3
±1
±2
±3
±9



(° C.)
23.3
24.4
25.3
24.0
24.3
25.3




±0.2
±0.1
±0.1
±0.1
±0.1
±0.1


DBO5(sol)
(mg/L)
380
490
470
450
500
470


DCOtot
(mg/L)
1480
1920
1520
3050
2310
2330




±80
±130
±100
±240
±70
±90


DCOsol
(mg/L)
1190
1010
965
960
968
944




±160
±210
±21
±24
±57
±11


MES
(mg/L)
367
422
719
1181
485
752




±240
±126
±457
±308
±175
±316


MVS
(mg/L)
354
410
706
1160
461
717




±207
±126
±454
±270
±201
±304


PO43−
(mg/L)
0.61
0.55
0.54
0.53
0.57
0.47




±0.06
±0.03
±0.01
±0.01
±0.02
±0.02


NH4+
(mg/L)
0.23
0.14
0.01
0.01
0.02
0.00




±0.02
±0.11
±0.01
±0.01
±0.02
±0.00









EXAMPLE 4

Solid waste from a pulp plant were subjected to a treatment with the apparatus of the present invention. The results are set forth in Table 4 hereinbelow.
















Control
Treated














Parameters
Units
Not Treated
No gas
Air
O2
CO2
N2

















pH

5.83
5.95
6.04
5.97
4.79
5.89




±0.04
±0.03
±0.03
±0.02
±0.01
±0.03


POR
(mV)
−113
−55
6
23
27
−65




±11
±7
±12
±6
±1
±4



(° C.)
21.9
25.7
26.6
27.1
25.6
24.9




±0.3
±0.1
±0.1
±0.2
±0.1
±0.1


DBO5(sol)
(mg/L)
430
410
420
450
330
690


DCOtot
(mg/L)
N/A
N/A
N/A
N/A
N/A
N/A


DCOsol
(mg/L)
624
947
1050
901
1200
1020




±42
±42
±20
±50
±140
±30


MES
(mg/L)
23500
17500
15800
16600
14700
17700




±400
±1500
±200
±600
±600
±2000


MVS
(mg/L)
22500
16800
15100
15900
14100
16900




±400
±1400
±200
±500
±500
±1900


PO43−
(mg/L)
14.3
14.1
13.8
13.7
13.8
15.1




±0.2
±0.3
±0.5
±0.2
±0.4
±0.1


NH4+
(mg/L)
3.97
8.03
8.24
8.06
7.57
8.61




±0.33
±0.42
±0.65
±0.43
±1.24
±0.38









EXAMPLE 5

Liquid hog manure was subjected to a treatment with the apparatus of the present invention in the manner set forth in the previous examples. The results are set forth in Table 5 hereinbelow.















Treated














Parameters
Units
Control Not Treated
No gas
Air
O2
CO2
N2

















pH

7.33
7.62
7.70
7.97
6.96
7.84




±0.02
±0.01
±0.03
±0.02
±0.01
±0.02


POR
(mV)
−320
−163
−165
−5
−152
−283




±6
±25
±42
±1
±36
±6



(° C)
17.0
20.7
22.0
22.2
22.7
22.9




±0.3
±0.2
±0.5
±0.2
±0.2
±0.1


DCOtot
(mg/L)
36100
34900
34600
35300
32300
35900




±1200
±500
±1400
±1200
±1900
±1900


DCOsol
(mg/L)
9290
17700
12500
12600
14000
13500




±290
±200
±100
±700
±400
±100


MES
(mg/L)
20800
17200
18800
19600
19100
21900




±600
±500
±100
±200
±200
±100


MVS
(mg/L)
14000
11300
11300
12800
12400
14700




±400
±500
±100
±200
±200
±100


PO43−
(mg/L)
205
161
158
152
190
181




±6
±8
±2
±6
±18
±43


NH4+
(mg/L)
3180
2160
2170
2250
2280
2230




±240
±20
±120
±30
±40
±70


Ptot
(mg/L)
732
609
643
618
659
628




±33
±11
±40
±74
±52
±92


NTK
(mg/L)
3010
2540
3400
2930
3160
3710




±240
±80
±70
±210
±130
±620









The DCO sub-total was slightly diminished while the DCO total was substantially increased. The level of the phosphates and ammonium were also decreased. A decrease in the odor was also noted with a substantial decease being obtained with the use of oxygen.


EXAMPLE 6

A synthetic multi-metallic effluent was subjected to a treatment with the apparatus of the present invention. The results are set forth in Table 6 hereinbelow.
















Control
Treated















Parameters
Units
White
Not Treated
No gas
Air
O2
CO2
N2


















pH

N/A
2.17
2.17
2.21
2.07
2.34
2.27





±0.02
±0.01
±0.05
±0.02
±0.02
±0.01


POR
(mV)
N/A
487
516
493
518
499
476





±4
±5
±8
±2
±3
±3



(° C.)
N/A
25.9
26.6
25.8
27.4
27.9
23.8





±0.1
±0.1
±0.1
±0.3
±0.1
±0.1


Al
(mg/L)
0.01
0.51
0.88
0.44
0.43
0.41
0.54




±0.01
±0.03
±0.03
±0.04
±0.03
±0.05
±0.03


Ca
(mg/L)
0.19
18.3
28.2
16.5
16.1
17.6
19.1




±0.10
±0.5
±0.5
±0.9
±1.6
±1.4
±0.4


Cd
(mg/L)
0.00
12.6
10.2
10.6
10.8
11.1
12.3




±0.00
±0.5
±0.7
±0.4
±0.7
±0.8
±0.2


Cr
(mg/L)
0.00
1.92
1.57
1.63
1.65
1.70
1.91




±0.00
±0.10
±0.12
±0.06
±0.11
±0.12
±0.04


Cu
(mg/L)
0.11
5.13
30.2
29.1
20.1
15.7
12.5




±0.00
±0.36
±2.1
±1.2
±0.8
±1.1
±0.3


Fe
(mg/L)
0.20
54.1
13.6
22.1
26.7
29.9
80.8




±0.01
±29.1
±0.2
±0.8
±1.9
±2.4
±1.8


Mg
(mg/L)
0.05
12.7
14.3
11.2
11.2
11.6
12.8




±0.01
±0.5
±1.6
±0.5
±0.7
±0.8
±0.3


Mn
(mg/L)
0.00
3.55
2.84
2.98
3.02
3.10
3.57




±0.00
±0.23
±0.23
±0.13
±0.18
±0.23
±0.07


Na
(mg/L)
0.09
53.8
57.7
45.4
46.6
48.0
53.4




±0.05
±2.5
±7.7
±2.1
±2.9
±3.5
±1.3


Ni
(mg/L)
0.00
3.48
2.99
3.02
3.05
3.08
3.47




±0.00
±0.18
±0.22
±0.12
±0.20
±0.22
±0.06


Pb
(mg/L)
0.02
35.0
36.9
34.9
32.7
33.5
35.4




±0.00
±1.6
±2.5
±1.1
±1.9
±2.2
±0.9


Zn
(mg/L)
0.06
7.40
18.1
12.3
9.37
8.88
8.90




±0.01
±0.67
±1.5
±0.5
±0.62
±0.64
±0.15









As will be noted, there were varying results depending upon the particular metal which was to be removed.


EXAMPLE 7

A male beagle dog followed by inhalation of a mixture of isoflurane, nitrous oxide and oxygen. The oxygen supply was gradually reduced to approximately 60% SpO2. The femoral artery and cephalic vein were cauterized to provide lines for arterial and venous blood sampling. The animal was administered intravenously sodium chloride with stabilized dissolved oxygen at a dose concentration of 33 ppm and dose volume of 500 ml. The results are given in Table 7 hereinbelow.
















Animal

SpO2
pO2
Sampling


No.
Occasions
%
mmHg
Site for pO2







1001A
Pre-Dose
49
26
Venous



Pre-Dose
49
25
Arterial



Immediately Post-Dose End
48
27
Venous



Immediately Post-Dose End
48
25
Arterial



10 min Post-Dose End
49
25
Venous



10 min Post-Dose End
49
26
Arterial



15 min Post-Dose End
49
25
Venous



20 min Post-Dose End
49
28
Arterial



30 min Post-Dose End
55
27
Venous



35 min Post-Dose End
56
29
Arterial



40 min Post-Dose End
58
29
Venous



45 min Post-Dose End
58
32
Arterial



50 min Post-Dose End
60
32
Venous



55 min Post-Dose End
61
32
Arterial



60 min Post-Dose End
61
30
Venous



65 min Post-Dose End
61
34
Arterial



70 min Post-Dose End
62
34
Venous



75 min Post-Dose End
64
39
Arterial



80 min Post-Dose End
63
**
Venous



85 min Post-Dose End
62
34
Arterial



90 min Post-Dose End
64
**
Venous



95 min Post-Dose End
62
39
Arterial



100 min Post-Dose End
65
37
Venous



105 min Post-Dose End
67
38
Arterial



110 min Post-Dose End
67
37
Venous



115 min Post-Dose End
66
37
Arterial



120 min Post-Dose End
66

Venous



125 min Post-Dose End
65
37
Arterial



130 min Post-Dose End
64
35
Venous



135 min Post-Dose End
64
35
Arterial



140 min Post-Dose End
63
35
Venous



145 min Post-Dose End
64
37
Arterial



150 min Post-Dose End
65

Venous



155 min Post-Dose End
65
38
Arterial



160 min Post-Dose End
64
38
Venous



170 min Post-Dose End
68

Venous



175 min Post-Dose End
66

Venous



185 min Post-Dose End
67
40
Arterial



190 min Post-Dose End
65
**
Venous



195 min Post-Dose End
65
**
Arterial



200 min Post-Dose End
66
35
Venous



205 min Post-Dose End
65
39
Arterial





—: Unable to obtain value


**: Value outside readable range






EXAMPLE 8

A male beagle dog, prepared according to Example 6, was administered orally reverse osmosis water with stabilized dissolved oxygen at a dose concentration of 100 ppm and a dose volume of 250 ml. The results are given in Table 8 hereinbelow.
















Animal

SpO2
pO2
Sampling


No.
Occasions
%
mmHg
Site for pO2



















1002B
15 min Pre-Dose
60
29
Venous



Pre-Dose
53
25
Arterial



5 min Post-Dose End
50
21
Venous



10 min Post-Dose End
53
16
Arterial



15 min Post-Dose End
59
19
Venous



20 min Post-Dose End
56
16
Arterial



25 min Post-Dose End
56
15
Venous



30 min Post-Dose End
97
223
Arterial









EXAMPLE 9

In this example, the male beagle dog was administered orally stabilized dissolved oxygen in a reverse osmosis water at a concentration of 100 ppm and a volume of 100 ml. The results are set forth in the Table 9 hereinbelow.
















Animal

SpO2
pO2
Sampling


No.
Occasions
%
mmHg
Site for pO2







1003C
Pre-Dose
58
29
Arterial



Pre-Dose
60
30
Venous



5 min Post-Dose End
73
47
Venous



10 min Post-Dose End
75
51
Arterial



15 min Post-Dose End
79
47
Venous



20 min Post-Dose End
85
51
Arterial



25 min Post-Dose End
84
53
Venous



30 min Post-Dose End
82
56
Arterial



35 min Post-Dose End
81
52
Venous



40 min Post-Dose End
84
54
Arterial



45 min Post-Dose End
82
54
Venous



50 min Post-Dose End
87
57
Arterial



55 min Post-Dose End
84
52
Venous



60 min Post-Dose End
83
56
Arterial



65 min Post-Dose End
81
54
Venous



70 min Post-Dose End
84
58
Arterial



75 min Post-Dose End
79
52
Venous



80 min Post-Dose End
81
48
Arterial



85 min Post-Dose End
82
61
Venous



90 min Post-Dose End
86
57
Arterial



95 min Post-Dose End
90

Venous



100 min Post-Dose End
79
46
Arterial



105 min Post-Dose End
84

Venous



110 min Post-Dose End
80
52
Arterial



115 min Post-Dose End
77

Venous





—: Unable to obtain value






EXAMPLE 10

Human subjects were administered reverse osmosis water having a stabilized dissolved oxygen of 100 ppm. The blood oxygen level was then measured at varying time intervals. The results are set forth in FIGS. 4 to 10.


As will be noted, in all instances, the blood level oxygen increased and remained increased for varying periods of time.

Claims
  • 1. In a method for fixing a first fluid within a second fluid comprising the steps of mixing said first and second fluids together; the improvement comprising the steps of passing said fluid between two electrodes, a first one of said electrodes (105, 110, 115) being formed of a metallic material having a dielectric covering (106, 111, 116) thereon, a second one of said electrodes (107, 112, 117) being formed of a metallic material and being grounded; and applying a DC voltage (2) to said first one of said electrodes (105, 110, 115), said fluids being passed spirally through a treatment zone where said fluids are subjected to an electric field from said DC voltage.
  • 2. The method of claim 1 wherein said voltage is more than +/−10 kV.
  • 3. The method of claim 2 wherein said first fluid is a gas.
  • 4. The method of claim 3 wherein said second fluid is a liquid.
  • 5. The method of claim 4 wherein said first fluid is oxygen and said second fluid is water.
  • 6. The method of claim 2 wherein said electric field has a voltage of at least ±15 kV.
  • 7. The method of claim 2 wherein said first fluid is a gas and said second fluid is a gas.
  • 8. The method of claim 2 wherein said fluid is for human consumption.
  • 9. The method of claim 8 wherein said first fluid is oxygen and said second fluid is a fruit juice.
  • 10. The method of claim 8 wherein said first fluid is oxygen and said second fluid is milk.
  • 11. The method of claim 2 wherein said first fluid is oxygen and said second fluid is a flowable resin.
  • 12. The method of claim 1 wherein said first fluid is a liquid and said second fluid is a liquid.
Priority Claims (1)
Number Date Country Kind
2320014 Sep 2000 CA national
Parent Case Info

This application claims the benefit of Provisional Applicational No. 60/200,135 filed Apr. 27, 2000.

PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/IB01/00701 4/27/2001 WO 00 10/25/2002
Publishing Document Publishing Date Country Kind
WO01/81246 11/1/2001 WO A
US Referenced Citations (10)
Number Name Date Kind
4175871 Suh et al. Nov 1979 A
4508265 Jido Apr 1985 A
5762775 DePaoli et al. Jun 1998 A
5769155 Ohadi et al. Jun 1998 A
5814222 Zelenak et al. Sep 1998 A
6265025 DePaoli et al. Jul 2001 B1
6284293 Crandall et al. Sep 2001 B1
6451208 Ledoux Sep 2002 B1
20010050881 Depaoli et al. Dec 2001 A1
20030086333 Tsouris et al. May 2003 A1
Foreign Referenced Citations (1)
Number Date Country
WO 9950186 Oct 1999 WO
Related Publications (1)
Number Date Country
20030133354 A1 Jul 2003 US
Provisional Applications (1)
Number Date Country
60200135 Apr 2000 US