Chemtrail Patents: United States Patent 4,686,605 Source
United States Patent 4,686,605 / Eastlund / August 11, 1987
United States Patent 6,315,213 / Cordani / November 13, 2001.
United States Patent / 5,286,979 / Berliner / February 15, 1994
This invention is a process for absorbing ultraviolet radiation in the atmosphere by dispersing melanin, its analogs, or derivatives into the atmosphere. By appropriate choice of melanin composition, size of melanin dispersoids, and their concentration, the melanin will absorb some quantity of ultraviolet radiation and thereby lessen its overall effect on the critters who would normally absorb such radiation. ***continue
Liquid atomizing apparatus for aerial spraying
United States Patent / 4,948,050 / Picot / August 14, 1990
A rotary liquid spray atomizer for aerial spraying is driven by a variable speed motor, driven in turn by power from a variable speed AC generator. The generator is driven from a power take-off from the engine of the spraying aircraft, a drive assembly includes a device for controlling the speed of the generator relative to the speed of the engine. The particularly convenient drive assembly between the generator and the power take-off is a hydraulic motor, which drives the generator, driven by a hydraulic pump driven from the power take-off. The speed of the hydraulic motor can be controllably varied. Conveniently the AC motor is a synchronous motor. ***continue
Laminar microjet atomizer and method of aerial spraying of liquids
United States Patent / 4,412,654 Yates / November 1, 1983
A laminar microjet atomizer and method of aerial spraying involve the use of a streamlined body having a slot in the trailing edge thereof to afford a quiescent zone within the wing and into which liquid for spraying is introduced. The liquid flows from a source through a small diameter orifice having a discharge end disposed in the quiet zone well upstream of the trailing edge. The liquid released into the quiet zone in the slot forms drops characteristic of laminar flow. Those drops then flow from the slot at the trailing edge of the streamlined body and discharge into the slipstream for free distribution. ***continue
Rocket having barium release system to create Ion clouds in the upper atmosphere.
United States Patent: – US3813875 / Issued/Filed Dates: June 4, 1974 / April 28, 1972
A chemical system for releasing a good yield of free barium (Ba°) atoms and barium ions (BA+) to create ion clouds in the upper atmosphere and interplanetary space for the study of the geophysical properties of the medium. Inventor(s): Paine; Thomas O. Administrator of the National Aeronautics and Space Administration with respect to an invention of , Hampton, VA 23364 ***continue
NASA: BARIUM – Chemical Formulas/Suppliers – source: gisgaia
This is the “Description of Preferred Embodiments” link in the NASA Barium Patent listed above. Astounding that this information was generated in l969 and now, 30 years later, there is evidence of Barium saturation in our atmosphere.
The Barium/Fuel mixtures are listed below along with the suppliers.
Description of Preferred Embodiments:
Referring now to the drawings and more particularly to FIG. 1, there is shown a segment of a suitable carrier vehicle 10, such for example a rocket motor. Vehicle 10 is employed to carry fuel tank 11, insulated oxidizer tank 13 and combustion chamber 15, along with the necessary instrumentation, from earth into the upper atmosphere or into interplanetary space. Fuel tank 11 is in fluid connection with combustion chamber 15 and oxidizer tank 13 is in fluid connection with combustion chamber 15 by way of respective conduits 17 and 19. A pair of valves 21 and 23 are disposed within the respective conduits 17 and 19. Valves 21 and 23 are adapted to be selectively and simultaneously opened by a suitable battery-powered timing mechanism, radio signal, or the like, to release the pressurized fuel and oxidizer from tanks 11 and 13. The fuel and oxidizer then flow through conduits 17 and 19 and impinge upon each other through a centrally positioned manifold and suitable jets (not shown) in combustion chamber 15 where spontaneous ignition occurs. The reaction products are then expelled through the open ends of combustion chamber 15 as plasma which includes the desired barium neutral atoms and barium ions as individual species.
The fuel utilized in fuel tank 11 is either hydrazine (N2 H4) or liquid ammonia (NH3) while the oxidizer employed is selected from the group consisting of liquid fluorine (F2), chlorine trifluoride (ClF3) and oxygen difluoride (OF2). When using hydrazine as the fuel, barium may be dissolved therein as barium chloride, BaCl2, or barium nitrate, Ba(NO3)2, or a combination of the two. When using liquid ammonia as the fuel, barium metal may be dissolved therein. The combination found to produce the highest intensity of Ba° and Ba+ resonance radiation in ground based tests involved a fuel of 16 percent Ba(NO3)2, 17 percent BaCl2 and 67 percent N2 H4 ; and as the oxidizer, the cryogenic liquid fluorine F2 and in which an oxidizer to fuel weight ratio was 1.32.
Other combinations of ingredients tested are set forth in Table I below:
TABLE I
______________________________________
System Optimum O/F Percent
Ionization
Calculated
______________________________________
16.7% BaCl2 –
83.3% N2 H4 /ClF3
2.36 68.0
26% BaCl2 –
74% N2 H4 /ClF3
2.08 70.0
50% Ba(NO3)2 –
50% NH3 /ClF3
1.52 –
42.9% Ba(NO3)2 –
57.1% N2 H4 /ClF3
1.19 50.0
16.7% BaCl2 –
83.3% N2 H4 /F2
1.95 68.8
26% BaCl2 –
74% N2 H4 /F2
1.71 70.6
21% BaCl2 –
9% Ba(NO3)2 –
70% N2 H4 /F2
1.57 68.5
17% BaCl2 –
16% Ba(NO3)2 –
67% N2 H4 /F2
1.31 68.1
13% BaCl2 –
21.5% Ba(NO3)2 –
65.5% N2 H4 /F2
1.34 63.7
9% BaCl2 –
30% Ba(NO3)2 –
61% N2 H4 /F2
1.04 63.7
42.9% Ba(NO3)2 –
57.1% N2 H4 /F2
0.976 43.0
42.9% Ba(NO3)2 –
57.1% N2 H4 /OF2
0.694 46.9
26% BaCL2 –
74% N2 H4 /OF2
1.22 52.8
______________________________________
The conditions under which each of the combinations listed in Table I were tested were ambient and the percentage ionization was calculated by equations set forth in NASA Contract Report CR-1415 published in August 1969.
.
The chemical supplier and manufacturers stated purity for the various chemicals employed are set forth in Table II below:
______________________________________
Chemical
Supplier Purity
______________________________________
N2 H4
Olin Mathieson Chemical
Technical Grade
Company, Lake Charles,
97-98% N2 H4
Louisiana (2-3% H2 O)
NH3
Air Products and Chemicals
Technical Grade
Allentown, Pa.
BaCl2
J. T. Baker & Co. Reagent Grade
Phillipsburg, N.J.
Ba(NO3)2
J. T. Baker & Co. Reagent Grade
Phillipsburg, N.J.
F2 Air Products & Chemicals
98%
Allentown, Pa.
ClF3
Allied Chemical Co.
99.5%
Baton Rouge, La.
OF2
Allied Chemical Co.
98%
Baton Rouge, La.
.______________________________________
A solubility study of various mixtures containing Ba(NO3)2, BaCl2 and N2 H4 was made at room temperature and is shown in the triangular plot of FIG. 2. Seven solutions that were used in the tests enumerated in Table I are indicated by reference letters in FIG. 2 as follows:
a. 16.7% BaCl2 – 83.3% N2 H4
b. 26% BaCl2 – 74% N2 H4
c. 21% BaCl2 – 9% Ba(NO3)2 – 70% N2 H4
d. 17% BaCl2 – 16% Ba(NO3)2 – 67% N2 H4
e. 13% BaCl2 -21.5% Ba(NO3)2 -65.5% N2 H4
f. 9% BaCl2 – 30% Ba(NO3)2 – 61% N2 H4
g. 42.9% Ba(NO3)2 – 57.1% N2 H4
A mixture below the Saturation Line, that is toward the Ba(NO3)2 or BaCl2 corners contained a solid and a solution phase whereas the salts were in complete solution above the saturation line.
.
All fuel mixtures or systems described were easily handled except the 50 percent Ba(NO3)2 -50 percent NH3 system. This system caused clogging of the feed valves due to precipitation of the Ba(NO3)2. In addition the light values obtained using this system was relatively low.
.
In testing of each of the fuel mixtures set forth in Table I the Ba° light was greater than the Ba+ light for a given oxidizer/fuel ratio in each of the mixtures. The maximum light occurred in all systems at a point located between the stoichiometric O/F and 3 percent less than the stoichiometric O/F. The stoichiometric O/F is defined as being equivalent to the oxidizer to fuel weight ratio in a balanced equation assuming the salt is converted to free Ba, F to HF, Cl to HCl and O to H2 O. For example, one system tested had an O/F ratio of 142 grams oxidizer per 100 grams fuel or 1.42/1.00. If the barium is assumed to be converted to BaF2 then the stoichiometric O/F is 1.47. Since the greatest light output in all cases occurred with O/F less than stoichiometric it is apparent that little of the Ba was combined as BaF2 or BaCl2. This was confirmed by spectrographic analysis.
In Table II the various systems are listed in decreasing light output or relative light intensity as measured by phototubes in millivolts, thereby indicating the relative barium yield.
__________________________________________________________
SYSTEM MAXIMUM RELATIVE
(percent weight for fuel)
INTENSITY, millivolts
Ba° 5535 A
Ba+ 4554 A
___________________________________________________________
17% BaCl2 -16% Ba(NO3)2 -67% N2 H4 /F2
27600
11800
13% BaCl2 -21.5% Ba(NO3)2 -65.5% N2 H4 /F2
23600
8340
21% BaCl2 -9% Ba(NO3)2 -70% N2 H4 /F2
20600
9100
9% BaCl2 -30% Ba(NO3)2 -61% N2 H4 /F2
16600
5970
26% BaCl2 -74% N2 H4 /F2
16600
6520
26% BaCl2 -74% N2 H4 /OF2
11800
2100
16.7% BaCl2 -83.3% N2 H4 /F2
9100 3350
42.9% Ba(NO3)2 -57.1% N2 H4 /F2
9000 1800
42.9% Ba(NO3)2 -57.1% N2 H4 /OF2
7300 1330
42.9% Ba(NO3)2 -57.1% N2 H4 /ClF3
663 94
50% Ba(NO3)2 -50% NH3 /ClF3
221 44
___________________________________________________________
- PATENT #: 4873928 - October 17, 1989 – Nuclear-sized explosions without radiation
- PATENT #: 3994437 – November 30, 1976 – Broadcast dissemination of trace quantities of biologically active chemicals
- PATENT #: 6030506 – February 29, 2000 – Preparation of independently generated highly reactive chemical species.
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