Portable diver heat generating system

• US 4,223,661 A
• Filed: 08/13/1979
• Issued: 09/23/1980
• Est. Priority Date: 08/13/1979
• Status: Expired due to Term

• Current Assignee: James F. Jenkins, Sergius S. Sergev, Stanley A. Black
• Original Assignee: James F. Jenkins, Sergius S. Sergev, Stanley A. Black
• Inventors: Jenkins, James F., Black, Stanley A., Sergev, Sergius S.
• Primary Examiner(s): Scott, Samuel
• Assistant Examiner(s): Green, Randall L.
• Application Number:
  US06/066,201
• Time in Patent Office: 407 Days
• Field of Search: 126/204, 126/263, 128/402, 165/46, 44/3 R, 44/3 B, 60/218, 60/219
• US Class Current: 126/204
• CPC Class Codes: B63C 11/28 Heating, e.g. of divers' suits, of breathing air

Abstract

Supercorroding magnesium alloys that react rapidly and predictably with seawater to produce heat and hydrogen gas. The alloys are formed by a mechanical process that bonds magnesium and noble metal powder particles together. The alloy powders can be sintered to form barstock, etc., suitable for self-contained corroding links.

Claims

1. A portable heat generating system, suitable for use with a diver water circulation garment, comprising:

a. a reaction chamber having an inlet and an outlet;

b. a heat exchanger chamber separate from and surrounding said reaction chamber;

c. said heat exchanger chamber having separate first and second sections;

d. the first section of said heat exchanger chamber having an inlet and outlet thereto through which a heating fluid is circulated;

e. a source of supercorroding mechanically alloyed powder;

f. means for supplying a controlled amount of said supercorroding alloy powder from said source to the inlet of said reaction chamber;

g. the second section of said heat exchanger chamber having an inlet and an outlet through which fresh seawater is circulated for preheating;

h. means for supplying a controlled amount of preheated seawater from the second section of said heat exchanger to the inlet of said reaction chamber where said seawater is mixed with said supercorroding powder for reaction thereof and high generation of heat;

the heat generated being substantially removed by the heating fluid and seawater circulated through said first and second chambers, respectively, of said heat exchanger chamber;

i. the cooled byproducts from the reaction of the seawater and supercorroding alloy powder being expelled from said reaction chamber outlet along with hydrogen.

2. A heat generating system as in claim 1 wherein the inlet and outlet from the first section of said heat exchanger chamber is connected to a heating load via circulation means;

the heating fluid being heated in said heat exchanger and circulated through said heating load by said circulation means.

3. A heat generating system as in claim 2 wherein means is provided to control the temperature to said heating load.

4. A heat generating system as in claim 1 wherein said supercorroding alloy powder is supplied from said source mixed with inert ingredients as a slurry.

5. A heat generating system as in claim 4 wherein said means for supplying said supercorroding alloy powder from said source is an externally pressurized bladder and a slurry flowrate controller.

6. A heat generating system as in claim 4 wherein said slurry is inert and of gel type consistency which facilitates pumping thereof.

7. A heat generating system as in claim 4 wherein said slurry consists in proportion by weight of:

magnesium based mechanically alloyed powder 447.0, methoxy polyethylene glycol 394.0, N-oco beta amino butyric acid 3.0, collodial silica at least 19.7, diethylenetriamine 1.0.

8. A heat generating system as in claim 1 wherein a seawater pump is provided to circulate water through said second section of the heat exchanger and into said reaction chamber.

9. A heat generating system as in claim 1 wherein said heating fluid through the first section of said heat exchanger counter flows the direction of flow of reactants through said reaction chamber.

10. A heat generating system as in claim 1 wherein 95 percent or more of the heat of reaction is produced in the portion of said reaction chamber which is surrounded by the first section of said heat exchanger, the balance of heat produced substantially occurring within the portion of said reaction chamber which is surrounded by the second section of said heat exchanger.