Yull Brown: Brown's Gas (Hyfuel); US Patent # 4,014,777

**[rexresearch.com](../../index.htm)**

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**Yull BROWN**

**HHO / Brown's Gas**

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**Hanissch Engineering Testimonial ( 12
March 1979 ) re: Brown's Gas**

![](hanisschbrownsgas1.png)  
![](hanisschbrownsgas2.png)  


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***Sunday Telegraph* (January 16, 1977)**



**"Browns Gas"**

A Sydney inventor has refused a giant American oil companys
offer to buy out his method of turning tap water into fuel. The
offer is one of more than a dozen Mr Yull Brown, of Auburn, has
received.

Mr Browns invention allows oxygen and hydrogen extracted from
ordinary tap water to be used safely for almost any type of
burning fuel. He envisages the day when cars, stoves, heating
and most of industry can be run on water or the gas extracted
from it. He has perfected his invention in a cutting and welding
torch, similar to an oxyacetylene torch, which is 30 times
cheaper than present torches and burns with a flame seven times
hotter.

Mr Brown says his company has spent more than $650,000 on the
invention, which has taken shape in his backyard workshop over
the past seven years.

"I will not sellout to any big company because they are all the
same, protecting their interests", he said. "People before have
had similar inventions to mine and they have sold out and
nothing has been heard of then inventions again".

**Alternate**

"I dont know whether the Americans want to buy it to use it or
to take it right of the market and protect their oil interests.

"I think that while there is a drop of oil left in the world
they will try to stop alternate power sources, so I will ignore
their offer.

"Companies that sell petrol and industrial gas have invested
millions of dollars in plant and steel bottles --- they dont
want to know about an invention that can use 10 gallons of water
to produce enough gas for 6 weeks work or to run a car".

Mr Brown said he would start producing commercial models of his
welding torch within the next couple of months while a company
in England did the same thing there.

He has patented his invention in 32 countries, and has entered
into a $500,000 agreement with the English firm for the
production of his cutting torch.

Mr Brown said the other offers --- from Britain and European
forms --- would be considered.

"Only one Australian firm has approached me since I announced
the perfection of my method last week, but I would like to see
all the other developments take place here".

The torches will incorporate an electric arc welder, will cost
about $1300, and will produce about 10 cubic feet of gas for
about 6 cents.

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***Australasian Post* (February 16, 1978)**

**[ No Author / Title Info Available ]**

The most talked-about inventor in Australia today is Yull Brown
of Sydney --- the man who uses ordinary water as the fuel for
all his inventions.

To non-scientific minds it must be a bit hard to swallow, but
its all perfectly true. Mr Brown, 55, has succeeded, among
other things, in running a Mazda car, and Holden car engine on
water fuel.

He worked as a laboratory technician for a while and later
branched into business son his own.

A few years ago, a group of seven businessmen put up $700,000
in a company called Water Fuel Holdings to finance Mr Browns
experiments.

But what was Mr Browns original inspiration to use water as a
fuel source? When we stop for a moment and consider the
possibilities of water-fuelled ships, cars, and even jumbo jets,
it all sounds like something for a Jules Verne novel --- and
that, in fact, is where Mr Brown got his idea.

In 1875, Jules Verne in his book *The Mysterious Island*,
wrote the following passage:

"Water decomposed into its primitive elements, and decomposed
doubtless by electricity, which will then have become a powerful
and manageable force. Yes, my friends, I believe that water will
one day be employed as a fuel".

And thats a fair assessment of how Mr Brown does it. He
produces his hydrogen-oxygen mixture by electrolytic
dissociation of water by electrolytic dissociation of water
under the action of DC electrical current.

He has also successfully demonstrated a new type of welder,
powered from energy derived from water that could very soon make
him a multi-millionaire.

Small wonder that a steady stream of scientists and electronics
experts from all over Australia have been beating a path to Mr
Browns modest laboratories in the outer Sydney suburb of
Auburn.

It seems that just about everyone with a scientific mind in
this country wants to know how Yull Browns inventions work...

A short, solidly-built man with powerful forearms, Mr Brown is
aware that his inventions are bound to create a lot of enemies
in big business if and when they are ever launched into
commercial use.

"Some businesses stand to lose millions when my inventions are
accepted", he said, "so it would be a simple matter for them
topay some gangster $10,000 and get me put out of the way.

"I used to carry a pistol in a holster on my belt until a few
weeks ago. The police saw me wearing it on a television
interview and they came around the next day and took it away
from me. All Ive got to protect me now is my German Shepherd
called Ali Baba".

He separates the two gases by passing an electric current
through water, and has devised a way of storing them, as a
mixture, with no more danger than in the handling and storing of
other fuels.

Australian experts who have examined Mr Browns work have
agreed that he has made a notable breakthrough in the field of
oxy-hydrogen experiments.

---

***Imagine Magazine* (1988)**

**"New Alchemy --- Water Into Fire"**

**by Paul White**

Yull Brown is the man responsible for that popular urban myth
of the car that runs on water. When he first developed his new
water electrolysis process in the mid-70s he found a safe,
non-explosive method of separating water into oxygen and
hydrogen. He built a device that converted his car to run on the
hydrogen from water, with oxygen as the only exhaust emission.
He was shown on television at the time actually filling his car
with an ordinary garden hose!

A skeptical world was amused by the oddball news snippet. Then
Mr Brown began to have problems. He was, of course, loudly
denounced as a crank. Scientific experts were quoted as saying
the new technology was "physically impossible" and "ludicrous".
Absolutely no one would give him a research development load.
Approaches to the automobile industry only brought derision. His
bank foreclosed the mortgage on his home and, shortly
thereafter, he made television news again because of attempts
made on his life. Shots were fired into his kitchen.

Realizing that his new technology aroused the considerable
opposition of different corporations, Yull Brown disappeared
from public view with his water-car and set off on another track
to research and develop he new electrolysis process he had
discovered. The water-car became another urban myth along with
crocodiles in the sewers under the city.

Suddenly, last year, Mr Brown surfaces with a way of turning
water into fire.Under the corporate name of B.E.S.T Aust. Pty.
Ltd. He introduced a commercial range of revolutionary Gas
Generator Welders. Disposing completely with conventional
bottled gas, this new water-powered system generates a gas mix
called Browns Gas which produces a flame that can cut, fuse,
weld, solder and braze. Browns Gas has some remarkable
characteristics which include being able to weld a steel pipe to
brick with perfect molecular fusion!

The new company tried to float on the Sydney Stock Exchange for
development funds but a mysterious smear campaign of crank phone
calls defaming the product and claiming scientific documentation
that proved fraud so disturbed the Sponsoring Broker that
confidence was lost and all funds were returned to investors.
This year (1988), with the enthusiastic backing of a Korean
businessman, the company was floated again, quietly with a
minimum of fuss, on the Hobart Stock Exchange.

It may take a little while for the new technology to sink in
but Mr Brown reports an unprecedented avalanche of enquiries and
requests for information since the press reported his successful
bid on the Stock Exchange. The most startling claim by the
inventor in the press is that the gas produced in his process
can reduce nuclear and toxic waste to harmless carbon.

Mr Browns company is now in full production of the
revolutionary new welding machines, and is making first
deliveries. A larger version of the device is about to be
shipped to the USA where its ability to destroy plutonium and
other problem toxic wastes will be tested.

**The Technology**

In 1973, Prof Brown found that if hydrogen and oxygen were
carefully mixed in the same proportion found in water (two
hydrogen atoms to each oxygen atom) they would burn much more
safely. He developed the first high efficiency electrolysis cell
to produce his unique gas mix in a confined gas mix causes it to
implode rather than explode. It burns faster with higher
efficiency than any other gas mix. The flame front propagates at
3 km/second compared with only 10 m/sec for oxy-acetylene. This
means that with the gas burned at high pressure extremely
intense heat can be produced in a tiny volume.

In one instant the flame can be the temperature of a candle,
and you can wave your finger through it. Then, it will melt and
split granite or fuse metal pipes to house bricks. Browns gas
can reach 6000 degrees, the hottest known temperature. Tungsten,
the most heat-resistant metal which melts at 3600 degrees,
changes directly from a solid to a dark gas under the welder.

Mr Brown theorizes that the temperature of the flame is
determined at the surface of the material through an interactive
process between the hydrogen molecules and the atomic bonds in
the object being welded. Essentially, he argues, this is a
controlled thermonuclear reaction.

To use Browns gas as an energy source, it is detonated by a
spark which immediately forms a vacuum. Atmospheric pressure
then sucks water or any other liquid through a container or
hollowed area, electricity and water are the only elements
needed to activate and fuel the unit. Yull Brown has converted
the engine of his car to run on the mix. Atmospheric pressure
forces the pistons down into the cylinders to occupy the
near-vacuum caused by the implosion of the gas.

One wonders if the now much-mooted Greenhouse Effect might
break down the resistance of certain major corporations to
Browns gas generators being used to run cars and aircraft run
on water sooner rather than later. Indeed, this remarkable
Australian technology may have surfaced just in time to offer a
healthy alternative to present polluting power sources.

The water generator and welder have up to 30 different
applications covering the following technical areas: Glazing and
kiln operation, mining and mineral separation, drying of foods,
rocket fuel production, silica conversion, primary production,
irrigation, etc. Techniques are: Air-conditioning and cooling,
coal to oil conversion, pollution, smoke cleaning and
disintegration of toxic waste, cheap hydrogen production,
welding and brazing, liquid displacement, water pumps, graphite
production, industrial and somatic heating and cooking,
motor-cars, railways, ships, waste gas conversion, vacuum
systems, and the timber industry.

Dont look back but it looks as if the future may well have
arrived!

---

**Unidentified Text**

**"Yull Browns Gas"**

**Dr Browns Gas Production Differs From Electrolysis of Water**

The electrolysis method of separating water into its components
of hydrogen and oxygen is accomplished by passing an electric
current through water and is known since the early 1880s. Though
various methods of water electrolysis have been developed, these
require that the two gases, hydrogen and oxygen, are passed into
separate chambers due to the volatile nature of the gases when
mixed. If a volume of hydrogen is mixed with a volume of oxygen
in a percentage greater than 5%, a violent explosion occurs.
Likewise when oxygen is mixed with hydrogen. Water electrolysis
cells are generally not an efficient or economic source of
energy.

Browns proprietary process results in Browns Gas, a gas
containing ionic hydrogen and oxygen in proper mixtures which is
generated economically and safely and which can be compressed up
to 100 psi. It was first patented in Australia in 1977, with
patents granted in over 30 countries since. Six models of
generators are in production.

**Browns Gas Implodes to Vacuum + Water**

With his system, 1 kWh of electricity produces 340 liters of
gas. One unit of water yields 1866.6 units of the gas --- and
the inverse applies as well. Upon ignition, Browns Gas implodes
--- resulting in 1865.6 units of vacuum with one unit of water.
The end result of implosion is always pure water. The vacuum may
be generated in a device without moving parts.

**Thermal Effects of Browns Gas**

Standard blowtorches may be used to burn the gas, ignition
being obtained with a hot spark. Thermal energy is generated by
the interaction of ionic oxygen with the material coming in
contact, while the ionic hydrogen penetrates the material beyond
the oxidizing (heated) matrix domain, permitting a cooling
effect beyond. Browns Gas has achieved temperatures at above
6000 C --- the temperature of the sublimation of Tungsten (1/8"
diameter tungsten rod will vaporize within 30 seconds).
Evaluations show that Browns Gas welding is anywhere from 7.06
to 58.33% less expensive than oxy-acetylene gas welding,
depending on cost of electricity. The generators used for
welding purposes are manufactured by the major high-tech Chinese
manufacturing facility, NORINCO in Baotou, sold by Browns Gas
International Corp. in the USA.

**Ultra-Performance Fuel for Engines**

The February 9, 1978 Hansard of the New South Wales Legislative
and Legislative Assembly in Australia reports that Yull Brown
has driven his car 1,000 miles (1,600 kilometers) tone gallon of
water.

**Browns Gas for Deep-Space Life Support**

Browns Gas has been found to be of particular value in
replacing air, helium and oxygen for deep-sea breathing. It
permits doubling of the depth of manned diver penetration to
about 2,050 meters (over 6,750 feet) without narcosis effects,
and full working capacity despite the high pressures, as was
demonstrated in 16-day tests.

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***Planetary Association for Clean Energy*, Vol. 8(3)**

**"Browns Gas"**

**by Floyd Farley**

**Extracting Precious Minerals**

This report is strictly a preliminary report on using the flame
from Browns gas BN-200 Gas Generator extract complex Sonoran
Desert ores for assaying. It is in no way to be construed as a
final answer nor a methodology in the pretreatment or treatment
of ores for precious metal recovery.

Many months, if not years, of research still remain before any
real answers can be given with any degree of certainty as to the
effectiveness of the treatment of ores that exist in the world.

Tests completed to date by this writer are on ore from three
mines near Tonopah, AZ. They are: Hummingbird Group, Sierra
Associates, and Number Three Mine. Ore from all these mines were
known to contain gold, some silver, and the platinum group.
Silver, because of its low quantity and low price, has been
discounted in these tests. These ores are a complex of many
elements and compounds and have not been workable with any of
the commercial processes for recovery of precious metals.
Recovery can be made on the laboratory bench, but no commercial
process has been developed that will work. In addition, the
values in these ores cant be concentrated.

**Otherwise Economical Recovery**

The complexity of the ores causes them to be not amenable to
any type of fire assay, giving very little or no metals in the
cupel. Assays can be made with complex, uneconomical chemical
processes in the lab. Attempts to scale up with these processes
have been dismal failures.

Tests conducted by this writer and his associates initially
were with 1/6 assay ton samples. The flame was played across and
through the ores for different lengths of time and the changes
in colors and reactions were noted.

These samples were then fire-assayed using a straightforward,
common flux, crucible fusion, cupel method. Surprising results
occurred the first time with odd-looking odd-colored beads
remaining in the cupel. These beads were then weighed and pasted
with hot dilute nitric acid to expel silver, palladium, and
other unwanted metals. The remaining particles were again
weighted and digested in aqua regia.

**Successful, Enhanced Recovery**

The gold was then precipitated out and the residuals were again
put back in solution to digest the platinum and the rhodium and
the precipitants reduced to metal and weighed.

Metal recovery was consistent with the AA readings. The
chemical assay results were read on the AA and no attempt was
made to recover the metals, as the AA readings were consistent
with readings and recoveries from the fire assays. A third set
of tests has confirmed these results. A videotape is being made
that will show is being made that will show the methods used,
the reactions taking place and results.

The important discovery here is the ability after flame
treatment to use a straightforward fire assay to determine the
values in the ore. To this writers and to his associates
knowledge, this has never been done with any degree of certainty
or consistency. Also, never has the platinum from these ores
been this easy to get in hand as metal.

Gold values were somewhat lower (1.86 oz/ton) than previous
tests would indicate; however platinum (17.2 oz) and rhodium
were higher. These tests have proven what was known: that these
ores carry extremely good commercial values, even though no
process existed to extract them.

The next set of planned tests will attempt to determine dwell
time upon each of these ores for maximum assay recovery. Through
noted microscopic matrix changes in the ores, attempts to
concentrate the values will also be made.

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***Extraordinary Science* (October-December 1990)**

**"Browns Gas --- A Global Technological
Breakthrough"**

**by Robert Card**   
**Tomahawk Resources, Inc. (Vancouver, BC, Canada)**

**What is Browns Gas?**

Browns Gas is the product of the dissociation of water by
electrolysis, using the gas generator patented world wide by
Professor Yull Brown. It is a completely safe, compressed
stoichometric mixture of atomic and molecular hydrogen and
oxygen. It is colorless, odorless, lighter than air, and
non-toxic.

**Properties of Browns Gas**

Browns Gas burns with a clean flame. It will burn in a vacuum,
or under water. It uses no atmospheric oxygen, and creates only
pure water as its sole combustion product.

Browns Gas contains no hydrocarbons, and therefore is
incapable of producing carbon dioxide, or any other atmospheric
pollutant, when ignited.

Browns Gas cannot explode; indeed, it implodes upon ignition.
One liter of water produces 1860 liters of gas. When this gas is
ignited, the volume is reduced to the original one liter of
water. This characteristic is very useful in the creation of
near-perfect vacuums.

Browns Gas is produced from a very plentiful fuel, water, and
is may times less expensive than conventional bottled gas.

Very high temperatures are obtainable when Browns Gas is
ignited using a standard torch. Browns Gas is strongly ionized,
and exhibits many of the characteristics of plasma, at a small
fraction of the cost.

**Advantages of Browns Gas**

Browns Gas is derived from ordinary water, a plentiful and
readily available fuel, is safe and pollution-free, and presents
no hazard to the environment.

Due to its stoichometric nature, Browns Gas normally burns
with a perfectly neutral flame. This flame can be modified,
fluxed and switched from a reducing to an oxidizing flame at
extremely high frequencies.

The heat is highly concentrated, can be applied with extreme
accuracy and is axial in nature.

Browns Gas is produced on demand, where and when needed so no
storage is required. It can, therefore, be used in locations
where bottled gas is prohibited.

Since Browns Gas is lighter than air no dangerous
concentrations of gas are likely. Since it uses no oxygen from
the atmosphere, it can be used safely in closed spaces. Browns
gas is completely safe to generate and use, is pollution-free
and does not contribute in any way to the greenhouse effect.

All Browns Gas Generators are subject to a one-year guarantee
against defective materials and workmanship.

**Features of the Browns Gas Generator**

Browns Gas is supplied at 280-400 kpa (40-60 psi).

Browns Gas is produced at the rate of approximately 340 liters
per kilowatt of DC electricity.

Browns Gas Generators are fully safely, and are approved for
manufacture and use by the New South Wales Department of
Industrial Relations.

Have an automatic, fully regulated pressure system. They are
equipped with a pressure regulator, and pressure, voltage and
amperage gauges. Bo internal compressor is required, the gas is
generated and pressurized with no moving parts.

All units are compact, mobile, solidly constructed, with a
durable baked enamel finish.

The Browns Gas Generator is easily installed, as well as
simple and safe to operate.

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**Eagle Research Water Torches**

"The Eagle-Research 'ERxxxx WaterTorches' are superior to historical watertorches in most areas; including lower initial cost, long term reliability, efficiency of gas production, safety, ease of operation, small size, light weight and almost silent when producing gas.
  

    
    
 

"For technical questions, ordering
details, shipping quotes, etc. contact:**[watertorch@eagle-research.com](mailto:watertorch@eagle-research.com)**

"Eagle-Research is working with people around the world to
develop the Brown's Gas technology. This patent-free exchange of
information has resulted in an avalanche of progress in the
Brown's Gas research. Free cooperation has made tremendous
progress developing Brown's Gas machines that are far superior
to anything that has existed until now.

"For people who wish to find out more about Brown's Gas, a
large portion of the history and development of Brown's Gas
research is detailed in 'Brown's Gas, Book One'. It also gives
most of the mathematics needed to understand Brown's Gas and
the theory behind the Gas.

"'Brown's Gas, Book 2' contains all the needed information to
home-build a safe and easy to use commercial sized Brown's Gas
electrolyzer (several people have now done it, using surplus
components). The latter part of Brown's Gas, Book Two points out
some misconceptions and myths about Brown's Gas that that
Eagle-Research has been able to prove false with actual
experiments. However, Brown's Gas has many wonderful, beneficial
applications."... **www.eagle-research.com** (George
Wiseman).

---

**References**

*Nexus Magazine* ( US: PO Box 177, Kempton, IL
60946-0177, Ph: 815 253-6464 ~ Australia: PO Box 30, Mapleton,
Qld 4560, Ph: +61 (0)7 5442-9280 ~ Netherlands: PO Box 372,
Dronten 8250 AJ, Ph: +31 (0)3210 80558 ~ UK: 55 Queens Rd, East
Grinstead, W. Sussex, RH19 1BG, Ph: +44 (0)1342 322854 ) ~ Issue
No 7, Summer 1989, "Fire From Water" ~ Issue No 8, Autumn 1989,
"Jules Verne to Yull Brown, An Urban Myth Come True" ~ Issue No
9, 1989-1990, "Water Power--Fuel of the Future Today"

*Extraordinary Science Magazine* ( PO Box 5636, Colorado
Springs, CO 80931, Ph: 719-475-0918 ) ~ Vol 5 (3), Jul-Aug-Sep
1993, "Brown's Gas, A Revolutionary Breakthrough"

*Explore Magazine* ( PO Box 1508, Mt Vernon, WA 98273, Ph:
800-845-7866, 360-293-3282 ) ~  Vol 3 (2), 1992, "Fire From
Water, Saga of Yull Brown" (Part 1); Vol 3 (3), 1992, "Fire From
Water, Saga of Yull Brown" (Part 2) ~ Vol 3 (6), 1992, "Fire
From Water, Saga of Yull Brown" (Part 3)

*Planetary Association For Clean Energy* ( 100 Bronson
Ave, Suite 1001, Ottawa, Ontario, Canada, K1R6, Ph: 613 236-6265
) ~ Vol. 6, No 4, "Transmutations of Radioactive Materials with
Yull Brown's Gas"

*MaxaPower Technical Bulletin* (16625 Redmond Way,
Redmond, WA 98052 ) ~ "The Aqua-Phase Shift Technology 1991"

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**http://www.pureenergysystems.com/academy/papers/Common\_Duct\_Electrolytic\_Oxy-Hydrogen.htm**

**William A.Rhodes --- Common Duct Electrolytic Oxy-Hydrogen**
--- Claims precedence over Brown (Brown references Rhodes'
patents:USP # 3,262,872 and 3,310,483)

**KeelyNet** (04/11/02)

### "Difference between Rhodes Gas & Browns Gas" -

The following item was printed in the February 1998 PACE
(Planetary Association for Clean Energy) newsletter and is
followed by a response from Dr. William A. Rhodes, Yull Brown is
now deceased.

'An inventor who has been referenced before issuance of the
Yull Brown patents is now making claims on the Internet for
precedence for generation and single-ducted use of mixed atomic
hydrogen and oxygen. William A. Rhodes of the Arizona State
University, refers to his US patents 3,262,872 issued July 26,
1966 and 3,310,483 of March 21, 1977, about 5 years before Yull
Brown discovered his process in a small Sydney, Australia lab in
1971. Over 20 examiners, from Australia to the United Kingdom,
did not agree when they granted some 30 patents to Yull Brown in
the mid-1970s.   
The mixed gas produced by the Rhodes system is different and
does not have the unique - and for most conventional scientists
- 'anomalous' physical properties of Brown's gas. Essentially,
Brown's gas comes already mixed and compressed at determinable
levels, straight out of the electrolysis, while the Rhodes'
system is mixed in a 2:1 ratio after electolysis prior to
membranes and onto conduits and then to the torch.

Browns's gas burns in a vacuum, is subject to implosion - as a
single reaction - when sparked or heated, has a variable flame
temperature of about 138 C to over 6,000 C at which tungsten
sublimates and allows transmutation.

The Rhodes system allows for a production in 20, 75, 150 and
300 litres of mixed gas per hour. While 340 litres of Browns Gas
are generated per 1kwh, only 167 litres of the Rhodes mixed gas
are. The Rhodes system can use an 'outboard' alcohol booster
tank that increases BTU output while decreasing the flame
temperature of the standard 3,315 C to about 1,930 C.

The Rhodes system is manufactured by Arizona HydroGen
Manufacturing, 4225 East Madison Street, Phoenix, AZ 85034. It
has applications in welding, soldering, polishing and annealing
in industrial electronics, jewelry manufacturing, dental
laboratories, glass, ceramic and plastics industries. Details:
Dennis McMurray at 602-275-4126, FAX 267-8787.'

Date: Mon, 01 Apr 2002   
From: WILLIAM A. RHODES   
To: Jerry Decker   
TO: Planetary Association for Clean Energy

I am William Rhodes, whom your following newsletter was aimed
at.

Since my research documentation covering my invention of the
Single Ducted Oxy-Hydrogen system was complete on Keelynet (see
links below), I am puzzled by your statements. However, your
questions will be answered for correction further clarification
(Yours in quotes.):

"An inventor who has been referenced before issuance of the
Yull Brown patents is now making claims on the Internet for
precedence for generation and single-ducted use of mixed atomic
hydrogen and oxygen. William A. Rhodes of the Arizona State
University, refers to his US patents 3,262,872 issued July 26,
1966 and 3,310,483 of March 21, 1977, about 5 years before Yull
Brown discovered his process in a small Sydney, Australia lab in
1971."

\*\* I am \*now\* making claims? Look at Yull Brown's first U.S.
patent. My patent is clearly listed as a reference there and
dated 11 years prior to his. I used two years of experimenting
before going for a patent. \*\*

"Over 20 examiners, from Australia to the United Kingdom, did
not agree when they granted some 30 patents to Yull Brown in the
mid-1970s."

\*\* What did Examiners not agree on? Certainly it cannot be my
date of issuance or the invention itself? If not, then what? So
far, this dealt with non-applicable trivia. Many patent attor-
neys get jobs with the patent office because they were not
intel- ligent enough to remain in private practice. I have about
60 patents.

One case involved technology so strange I was attacked as a
fraud, and my application rejected. Time does not permit details
except to say, the invention was gross simplification of an
electrostatic generator using water dripping through two open
cans. It's predecessor existed for sale in an old Central
Scientific catalog. It contained four cans. I ripped out the
page and mailed it to the examiner with a note that said, "If I
am a fraud, then the company selling its equivalent is also a
fraud." US 2,742,58l patent issued immediately. Now, lets look
at more of your complaints.\*\*

"The mixed gas produced by the Rhodes system is different and
does not have the unique - and for most conventional scientists
- 'anomalous' physical properties of Brown's gas. Essentially,
Brown's gas comes already mixed and compressed at determinable
levels, straight out of the electrolysis, while the Rhodes'
system is mixed in a 2:1 ratio after electrolysis prior to mem-
branes and onto conduits and then to the torch."

\*\* I would certainly appreciate your explanation of what is
unique about Brown's Gas. I examined his patent and find nothing
different in his gas from mine. In either case compression of
such gases must not approach 400 psi where auto-ignition occurs.
Rhodes gas likewise comes straight from the electrolysis tank,
ALREADY MIXED, but NOT in a 2:1 ratio. It is a stoichiometric
mixture of 1:1 (atom for atom). A 2:1 ratio cannot be stoichio-
metric and would cause incomplete burning. There are no mem-
branes and "conduits". Mine is a single conduit. Whomever wrote
this either did not read, did not understand, or too hastily
scanned the document on Keelynet.\*\*

"Browns's gas burns in a vacuum, is subject to implosion --- as
a single reaction --- when sparked or heated, has a variable
flame temperature of about 138 C to over 6,000 C at which
tungsten sublimates and allows transmutation."

\*\* Excuse me! There is no scientific reason why any combustible
gas mixture chosen would not burn in a vacuum. This is an
oxymoron. The degree of vacuum is not mentioned. Not much of a
vacuum can exist with combustion occurring in it. The pumping
system merely sucks gases out the burner orifice. "Implosion?"
Implosion always occurs in both Brown and Rhodes. All hot gases
"implode" on a continuous basis, with continuous combustion. To
be proper, it should be called "volume shrinkage". When combus-
tion ceases, regardless of the gas species used the byproducts
of combustion and internal atmosphere SHRINKS toward ambient
pres- sure. This is just plain high-school physics, in open air
or partial vacuum. So far the author has a failing grade in
physics. This implosion myth has been circulating many years. It
comes from the scientifically ignorant. \*\*

"The Rhodes system allows for a production in 20, 75, 150 and
300 liters of mixed gas per hour. While 340 liters of Brown's
Gas are generated per 1kwh, only 167 liters of the Rhodes mixed
gas are. The Rhodes system can use an 'outboard' alcohol booster
tank that increases BTU output while decreasing the flame
temperature of the standard 3,315 C to about 1,930 C."

\*\* How was the liters per kw determined? The Rhodes
electrolyzer system delivers the maximum output from a proper
amount of potas- sium hydroxide (KOH). (Read the Keelynet
document again.) In the States, there are two manufacturers
claiming 100% efficiency. That, dear friend, would mean an
electrolyte with zero resist- ance, presently impossible. They,
including Yull Brown, were not aware that instruments used for
such measurements must be capable of accurately reading all
power delivered harmonics. Using the wrong instruments can and
does provide readings in excess of true energy used.

Example: If electrical energy is through a converter that
yields spikes occupying say 10% of the duty cycle, then false
readings can produce a miracle by showing an efficiency of 300%
or more. A gross impossibility. With that we would have, hooray,
over-unity -- free energy from nothing. (Yull Brown's higher gas
yields per 1kwh are no doubt instrument errors.) The only way to
determine true energy input vs BTU delivered is using a
watt/hour meter of the type seen on homes and businesses,
followed by a calorimeter. They read ALL energy, not just
portions of it. The last three sentences in the previous text
about the alcohol booster are almost correct.\*\* Instruments used
in compiling the original Keelynet document were NIST
calibrated. Nothing was left to chance. I would advise you read
and understand it before launching such ridiculous trivia as
found here. Somehow I touched a nerve yielding an emotional
response instead of a scientific one.\*\*

The Rhodes system is manufactured by Arizona HydroGen
Manufacturing, 4225 East Madison Street, Phoenix, AZ 85034. It
has applications in welding, soldering, polishing and annealing
in industrial electronics, jewelry manufacturing, dental
laboratories, glass, ceramic and plastics industries. Details:
Dennis McMurray at 602-275-4126, FAX 267-8787.'

Respectfully,   
William A. Rhodes, Physicist

**[Oxyhyd
1 paper](http://www.keelynet.com/energy/oxyhyd1.htm)**   
**[Oxyhyd 2
paper](http://www.keelynet.com/energy/oxyhyd2.htm)**

---

  
  
**US Patent  # 4,014,777**   
**March 29, 1977 ~ US Cl. 204/228.5**

**Welding**

**Yull Brown**

**Abstract ---** This invention relates to welding, brazing
or the like utilizing a mixture of hydrogen and oxygen generated
in substantially stoichiometric proportions in an electrolytic
cell by electrolytic dissociation of water, the mixture so
generated being passed from the generator through a flash-back
arrestor and thence to a burner where the gases are ignited. The
invention also relates to atomic welding in which the above
mentioned mixture is passed through an arc causing dissociation
of both the hydrogen and oxygen into atomic hydrogen and oxygen
which on recombination generate an intensely hot flame.

*Foreign Application Priority Data*   
Jul 20, 1973[AU] 4159/73   
May 02, 1974[AU] 7418/73   
Aug 03, 1973[AU] 4341/73

Current U.S. Class: 204/228.5; 204/268; 204/269; 204/270;
204/272; 429/21; 431/354   
Intern'l Class:  C25B 001/02; C25B 001/04   
Field of Search: 
204/129,270,278,228,230,237,269,229,272,271 136/86 R 55/3,100
29/498.5 219/137 431/354 206/.7

*References Cited*   
US Patent Documents   
685,274 ~ Oct., 1901 ~ Haas ~ Cl. 204/268.   
1,600,478 ~ Sep., 1926 ~ Lawaczeck ~ Cl. 204/272.   
3,045,665 ~ Jul., 1962 ~ Movat ~ Cl. 204/129.   
3,177,633 ~ Apr., 1965 ~ McDonald, Jr. ~ Cl. 55/3.   
3,262,872 ~ Jul., 1966 ~ Rhodes, et al. ~ Cl. 204/129.   
3,310,483 ~ Mar., 1967 ~ Rhodes ~ Cl. 204/129.

**Description**

This invention relates to welding, brazing and the like,
utilizing hydrogen and oxygen, and extends to such applications
as oxy-welding, oxy-cutting, atomic welding, and welding or
cutting in combination with electric arc techniques. The
invention also provides for the generation of hydrogen and
oxygen for the abovementioned applications in combination
therewith or separately.

A most important application of the invention is atomic welding
utilizing the properties of atomic oxygen in combination with
atomic hydrogen (for welding) or atomic oxygen separately (for
cutting). This particular application of the invention is based,
among other things, on the appreciation that considerable energy
is associated with the dissociation of molecular oxygen into
atomic oxygen by passing this gas through an arc, and that this
property can be usefully employed to generate temperatures even
higher than those previously attainable with, for example, an
atomic hydrogen flame. The significance of the energy which can
be obtained in this way can be appreciated from the following
reactions that take place, and the heat energies associated
therewith, when hydrogen and oxygen are both passed through an
electric arc. Thus:   
    \_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_   
    H.sub.2  H + H   
               
absorbing
101,000 cal. per gram mole   
    O.sub.2  O + O   
               
absorbing
117,000 cal. per gram mole   
               
total218,000
cal. per gram mole   
    \_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_\_

On recombination of these atoms this energy is released as heat
through a number of complex chemical reactions and results in an
extremely high flame temperature. Previously it would not have
been considered possible to practically pass oxygen or a mixture
of oxygen and hydrogen together through an arc due to the highly
explosive or inflammable nature of such gases. However in
accordance with the concepts of the present invention this is
indeed both possible and practical and, as mentioned above,
enables the realization of much higher welding or cutting
temperatures than hitherto obtainable by known practical means.

One of the objects of the present invention is to provide a
method and apparatus whereby hydrogen and oxygen can be
generated quickly and conveniently for immediate use for
welding, etc., without many of the disadvantages associated with
conventional gas welding practice. For example, the practice of
employing cylinders (or "bottles") of gas, usually oxygen and
acetylene can have significant disadvantages, particularly for
users working remote from a supply depot and for whom there
might be an appreciable delay between the placing of an order
for a delivery of gas the the actual delivery. For such users,
in order to ensure an adequate supply of gas when a particular
job demands it, it is often necessary to order fresh supplies in
advance, even before the supply on hand is fully used, or else
risk running out of gas before a job is completed. Since bottles
of gas are generally delivered on a strictly exchange basis --
in that a used bottle must be returned in exchange for a
refilled bottle -- the practice can mean a significant waste, as
far as the user is concerned, if bottles containing useful
amounts of unused gas have to be returned to the supplier.

The practice of using bottled gas also has associated with it a
large number of other problems such as the possibility of gas
leaking from bottles, possibility of industrial disputes which
can result in severe delays in delivery and in supply shortages,
liabilities, high purchase and storage costs, freight charges,
and so on.

To illustrate some of the conditions which the consumer of
bottled gas must put up with, listed below is a summary of the
"conditions of sale" which apply to the sale and distribution of
bottled gas.

a. The cylinder remains the sole property of the supplier,
which retains the right to exercise at any time its proprietory
powers in its discretion.

b. All cylinders and contents are forwarded at the expense and
risk of the customers.

c. It is the responsibility of the customers to provide
adequate labour for the loading and unloading of all cylinders
at the premises.

d. Cylinders are to be returned to the supplier as soon as
empty, carriage and freight charges paid.

e. A cylinder is not `returned` until received by the supplier
at its works or warehouse or by its truck and a receipt on the
suppliers form given for the same. No document purporting to be
a receipt for any such cylinder shall be valid unless it is the
suppliers printed form of receipt.

f. Cylinders are not transferable and must not be used for any
purpose other than as containers for the gas sold by the
supplier and must not be delivered or sent for recharging to any
place other than the suppliers gas station.

g. The customer agrees not to resell to any person or
Corporation, the gas contents of the cylinders of any part
thereof.

h. Customers are held responsible for all loss or damage to
cylinders from whatever cause arising from the time of delivery
until returned to the suppliers. (Customers are advised to cover
the cylinders by insurance).

i. Where a customer has not returned a cylinder in good order
and condition within six months from the date of delivery, the
supplier may, at its option, charge the customer with an amount
not exceeding the agreed value of the cylinder and the demurrage
due in respect thereof, and such amount is payable by the
customer as liquidated damages for the detention of the
cylinder. Notwithstanding the payment of such amount in respect
of any cylinder, it remains the property of the suppliers and
the right of the suppliers to recover possession thereof is not
affected in any way.

j. No allowance is made on any residual gas returned in the
cylinders.

k. And many other conditions varying in the different countries
in the world.

Another disadvantage, which is associated with oxy-hydrogen
welding arises due to the marked ability of hydrogen to be
absorbed by most metals. Thus when welding steel, for example,
great care must be taken to ensure that excess hydrogen is not
present otherwise it will be absorbed in the metal to cause loss
of strength and brittleness. On the other hand, an excess of
oxygen would cause burning of the metal and should thus equally
be avoided. It is most important therefore that with
oxy-hydrogen welding the mixture at the burner be adjusted to
produce a neutral flame, that is, one in which there is neither
excess hydrogen nor excess oxygen. In practice it is most
difficult to maintain (and virtually impossible to judge by
flame colour) a neutral flame, and for that reason oxy-hydrogen
welding is not widely used despite the inherent advantages of
low cost and high heat value offered by hydrogen as a fuel.

These and other disadvantages can be overcome to a significant
extent by the present invention whereby hydrogen and oxygen fuel
are generated simultaneously by electrolysis in an electrolytic
cell and allowed to freely mix therein to form a stoichiometric
mixture that will burn with a neutral flame. The fuel gas can be
generated where and whenever required thereby eliminating the
need for storage of bottles of gas and reliance on regular
deliveries of gas which often cannot be guaranteed.

The method of the present invention requires no diaphragms or
the like to separate the hydrogen and oxygen liberated by the
electrolysis process and thereby enables considerable advantages
to be realized over conventional electrolytic production of
these gases. Such diaphragms have normally been regarded as
essential for conventional electrolytic generators in order to
separate the two gases that would otherwise form a highly
explosive mixture; however, it has been found, in accordance
with the present invention, that the two gases can be safely,
and usefully, produced and utilized as a mixture for fuel
purposes provided that suitable safety precautions, such as the
employment of a flash-back arrestor, are taken. Such safety
precautions may include, for example, the employment of a device
which removes electrolyte vapour from the gas and at the same
time acts as a flash-back arrestor. In obviating the need for
diaphragms or the like the present invention enables the
electrodes to be placed much closer together and avoids the high
resistance associated with diaphragms, which in turn enables a
significant increase in the rate of gas production for a given
size of apparatus. In short the present invention enables the
manufacture of small size equipment that is useful for a large
variety of welding and similar work and that is not
prohibitively bulky for the average situation: something which
is impossible with conventional hydrogen-oxygen generating
equipment.

In the development of apparatus from the basic concept of
generation of hydrogen and oxygen electrolytically in a
practical manner suitable for large industrial applications on
the one hand, and small domestic applications on the other hand,
a number of factors had to be taken into account, analysed and
weighed one against the other. The following is a list of some
of these factors to illustrate what has been involved.

a. Endosmotic pressure to be balanced against the hydrostatic
pressure of the fluid.

b. Rate of flow of electric current in relation to the area of
the electrodes.

c. The prior art problem of removing the gases from anolyte and
catholyte, before diffusion and before the electrolytes are
intermixed.

d. Effects of rapid changes in the rate of flow of electricity
through the cell.

e. Effects of auxiliary decomposition within the anode and
cathode sides of the cell.

f. The choice of the most readily ionized electrolyte of a
maximum conductivity.

g. The least possible spacing between anode and cathode that
can be employed.

h. A design of cell in which previously it was regarded
impossible for the H.sub.2 and O.sub.2 given to become mixed
with safety, which does away with diaphragms or the like which
would increase the internal resistance, in which both hydrogen
and oxygen can be mixed within the cell, and in which cells can
be connected in series, parallel, or parallel and series to suit
requirements.

i. The choice of materials for the electrodes.

j. The quantity of acids or alkali to be used.

k. The shapes of cells according to purpose of the cells, and
the application for which they are designed.

l. The possibility of improvement with permanent or
electro-magnetically induced fields applied to the electrolytic
cells, to cause controlled separation of a quantity of the gases
generated in the cells.

m. Ensuring effective circulation of electrolyte between the
electrodes, with as little electrical resistance as possible.

n. The possibility of using sodium hydroxide or potassium
hydroxide which, in concentrations from 10% up to 30%, which has
negligible corrosion action on iron or nickel electrodes, apart
from producing a solution of good conductivity.

o. The use of the cooling effect by passing of hydrogen and
oxygen gases, for cooling electrolyte in the cell, for
controlling the cell temperature, preferably between 40.degree.
C to 60.degree. C, at which temperature the bonds between
hydrogen and oxygen need a minimum of electrical energy to
break.

g. The separation of hydrogen and oxygen from a mixture, using,
possibly, a permanent magnetic field, or an electro-magnetic
field which can be controlled to obtain a desired separation
between the hydrogen and oxygen. Based on this principle, the
oxygen could be substantially separated from the mixture and the
hydrogen could be absorbed by, for example, selected metals,
which have high absorption affinity for hydrogen (for example,
paladium which absorbs 900 times more hydrogen from its volume).
Also, using the principle of the invention, hydrogen and oxygen
can be generated in large quantities with small units and the
oxygen could, for example, be separated and used to supply
hospitals, baby rooms, air conditioning systems, or for any
other application, when oxygen is required. Oxygen can, in this
way, be generated much faster and more conveniently than with
conventional electrolytic generating equipment.

q. The possibility of absorbing the hydrogen or oxygen by
specially selected materials in small containers and where the
absorbed gas can be extracted when desired for welding or
brazing where it would be inconvenient or impossible to do so
with conventional equipment.

r. Making the welding operator entirely independent of any gas
suppliers.

s. The generation of cheap gas, up to 6 to 7 times cheaper than
normal gas supplies.

t. The design of equipment which gives not only professional
welders, but handymen, or people who would like to do welding at
home with oxy-welding apparatus, but would do it only
occasionally and could not justify the expense associated with
conventional gas supplies. Such people cannot justify paying for
bottles of gas for a single welding only (having to keep the
bottles, paying rent for them to keep them up to two years, to
perform the next welding). For this reason, the welding
apparatus made possible by the present invention is ideal
because it produces gases for welding at the time and in the
quantity that is needed.

u. Hydrogen-oxygen welding has the advantage that it does not
pollute the atmosphere as does oxy-acetylene welding.

v. The design of electrolytic cells which are safe to use as
well as convenient, which cells may incorporate their own
flash-back arrestors as a safety precaution or an equivalent
means, to prevent the hazards of explosion or fire.

w. The control of the current which passes through the cells,
the temperature of the cell, which is a function of current, the
control of the separation of the gases, and the removal from the
gases of electrolyte vapours. In this regard there has been
designed a special unit with preferably conical electrodes, and
a flash-back arrestor. The flash arrestor may be constituted by
a pellet of porous material, or a long capilliary pipe located
between the gas generator and a burner head. The fire hazards
associated with a mixture of hydrogen and oxygen cannot be
overemphasized and indeed it is probably mainly because of the
recognized dangers associated therewith that extreme lengths
have been taken to separate the two gases completely until they
reach the burner. In accordance with the present invention it
has been realized that, contrary to long standing opinions, the
gases can be safely mixed together even when being produced and
as a result many desirable advantages can be realized.

x. The provision of one or more safety valves adjusted to
convenient pressure for releasing excessive pressures in the
cell (for example, greater than 30 p.s.i.) which may result, for
example, if a current control mechanism fails. The safety valves
could be attached to an alarm, for example, to indicate a
failure in the current control mechanism or the cut-off
switches, etc.

y. Porous material may conveniently be placed in the burner
head, so that backfire through the burner into the cell cannot
occur.

In summary, the present invention contemplates, as an important
feature thereof, a universal welding apparatus capable of being
used to perform different types of welding operations based on
the utilization of hydrogen and oxygen, making full use of the
advantages which can thereby be realized, and equipment which
can be made small and portable compared with existing apparatus
such as that presently used for gas welding using bulky bottled
hydrogen. To generate the fuel, in accordance with the invention
a small compact electrolytic cell is made possible in which the
only raw material which has to be replenished from time to time
is water and which can be used whenever a source of electrical
energy is available to supply the necessary amount of hydrogen
or hydrogen and oxygen mixture for performing atomic welding or
hydrogen-oxygen flame welding. In its simplest form, the gas
generating apparatus of the present invention comprises an
electrolytic cell adapted to be connected to an energy source,
optionally through a step down transformer and rectifier, and
having means for connection to a burner, preferably through a
flash-back arrestor as a safety precaution.

The apparatus may be combined with a transformer as a single
compact unit and for convenience the transformer may be provided
with several windings to enable it to be used for auxiliary
purposes such as battery charging, electroplating, arc welding
or to provide an arc for atomic welding.

It has been found that a single electrolytic cell operating
without diaphragms at several hundred amps will generate
hydrogen and oxygen at a reasonable rate for small welding and
brazing work but for larger work (for example, the welding of 10
mm steel plate) the required amperage becomes excessive
(typically of the order of 900A or more) when considering the
size of conductors and transformer and the problem of heat
generation. Accordingly, in one aspect of the invention these
problems can be significantly reduced by arranging a plurality
of cells in series and using a much smaller current to obtain
the same effective gas output. In effect the capacity of a
series of cells for a given current input is that of a single
cell multiplied by the number of cells. Alternatively the
current requirement is reduced by a factor equal to the number
of cells -- for a given rate of gas production.

Even so a large number of separate cells can be excessively
bulky for portable applications and in a further aspect of the
invention, therefore, the bulk can be greatly reduced by
arranging the cells as a single unit in which a number of
electrodes, effectively in series, are arranged adjacent each
other in a common electrolytic chamber, the chamber being
provided with a gas collection space and an outlet for
connection to, for example, gas burner means. Furthermore, only
the end electrodes need be connected to an external source of
electrical energy and the arrangement as a whole can be made
extremely efficient and compact. Additionally the need for a
transformer for most applications can be eliminated by such an
arrangement so that the apparatus can be designed to be
electrically connected directly to a main electrical supply,
through a bridge rectifier if desired. By eliminating the need
for a transformer, the gas generating equipment as a whole can
be made surprisingly compact, to be well suited for small
domestic requirements as well as heavy industrial requirements.

In another important aspect of the invention, there is provided
a safety device which monitors the pressure of hydrogen and
oxygen being generated and regulates the current flowing through
the cell(s) to increase or decrease the rate of gas production
depending on the pressure. In one form the device comprises a
chamber containing two electrodes, at least one of which is
conical, arranged in the chamber (which normally contains a
conductive liquid) and the electrodes being connectable in
series with one or more electrolytic cells used for
oxygen-hydrogen production.

The pressure responsive, current regulating device can be
designed as an integral part of the electrolytic cell(s) or can
be used as an attachment connectable externally and in series
with the gas generating cell(s). The device can also be designed
to combine the functions of a current regulating device and a
flash-back arrestor, the latter function ensuring that a flame
at the burner does not accidentally pass back through the hose
lines to the highly explosive mixture in the gas generating
cell(s). The device may incorporate a total current cut-out
feature or may be used in combination with a cut-out device
which fully interrupts the supply of electrical power should the
pressure in the cell(s) accidentally exceed a maximum safe
value. The current regulating device may also operate to
regulate the current passing through the cells in accordance
with the temperature to maintain the temperature within a
desired range.

![](1.gif)

Referring to the drawings, FIG. 1 shows schematically a single
electrolytic cell 10 operating to produce a mixture of hydrogen
and oxygen, which mixture is passed through a flash-back
arrestor 11 to a burner 12. The cell 10 contains two plate
electrodes 10a and 10b immersed in an electrolyte consisting of
a solution of KOH in water and connectable through terminals 13
and 14 respectively to a source of a.c. or d.c. electricity.
Preferably, d.c. is used as the electrical impedance of the
cell, is much lower for d.c. than for a.c. The source of
electricity may be a transformer, typically of 300 Amps output
rating, connected to the cell through a bridge rectifier. The
flash-back arrestor 11 is constituted by a water bath in which
gas liberated in the cell 10 passes through a tube 15 into the
water bath 11 and thence through a tube 16 to the burner 12. The
arrangement is suitable for small welding and brazing work but
becomes too bulky for very large work.

![](2.gif)

FIG. 2 illustrates in vertical cross-section an electrolytic
cell 20 which requires a much lower current than the cell
illustrated in FIG. 1 for a given current input. The cell 20
comprises what is in effect a series of cells constituted by a
plurality of plate electrodes immersed in a solution of KOH in
water. For convenience the electrodes are designated as 20a for
the two electrodes at the ends and 20b for the intermediate
electrodes. The electrodes 20a are connected, via conductors 21
to terminals 22 for connection to an external supply of
electricity. The mixture of hydrogen and oxygen which is evolved
at the electrodes when an electric current is applied, passes
through an outlet opening 23 to a flash-back arrestor and thence
to a burner (not shown in FIG. 2). The series of electrodes 20a
and 20b are sealingly mounted in a tube 24 of insulating
material which is provided with restricted apertures 24a at the
top and 24b at the bottom, between each pair of electrodes. The
apertures 24a permit gas to escape into the space 25 above the
surface of the electrolyte and the apertures 24b permit
electrolyte to enter freely into the spaces between each pair of
electrodes. By virtue of this arrangement the electrical
resistance between any two adjacent electrodes is far less than
that between non-adjacent electrodes so that the arrangement is
effectively one of a large number of individual cells connected
in series. A very compact arrangement is therefore obtained but
one which permits a relatively high gas production rate for a
reasonably low current input. For example, a structure like that
shown, consisting of the equivalent of, for example, 120 cells
can generate gas at a current input of 15A (at, for example,
240V) equal to that of a single cell requiring a current input
of approximately 1800A. This means in practice that a relatively
portable apparatus can be produced which can be connected
directly, without a transformer, to most domestic electrical
supplies and which can maintain a sufficient rate of gas
production for most types of welding work.

An advantage which particularly distinguishes the arrangements
disclosed from conventional gas welding apparatus is that the
hydrogen and oxygen are automatically produced in substantially
the correct proportions to give a neutral flame. No mixing
valves are required and even unskilled personnel can produce
satisfactory welds without difficulty. In fact indications are
that many welds can be produced better than by any other welding
process.

![](3.gif)

FIG. 3 illustrates a pressure responsive safety device 30
operably connected in series (electrically) with an electrolytic
hydrogen-oxygen cell 31 for regulating the current passing
therethrough in accordance with the gas pressure being
generated. The device, or cell 30 comprises a chamber 30' in
communication with a reservoir 32 via a passage 33. Two conical
electrodes 34 and 35 are mounted in spaced relation within the
chamber and connected in series between a d.c. source (not
shown) and the electrolytic cell 31. An electrolytic solution of
KOH and water is provided within the chamber, portion of which
enters the reservoir 32. When the cell 31 is operating to
produce hydrogen and oxygen the pressure of the gas being
produced acts on the surface of the electrolyte in the chamber
30' to displace an amount of the electrolyte into the reservoir
32 against back pressure exerted by air trapped in the
reservoir, the amount of electrolyte displaced depending on the
pressure of the gas in the chamber 30'. At the same time the
area of contact between the electrodes and the electrolyte in
the cell 30 reduces in proportion to the drop in electrolyte
level, causing the electrical resistance of the cell 30 to rise
and the current passing therethrough to fall. Should the gas
pressure drop the electrolyte level in the cell 30 will rise and
the current passing into the cell 31 will also rise. Thus the
cell 30 operates to regulate the rate of gas production in
accordance with the pressure produced and prevents excess gas
pressure to build up in the cell 31.

![](4.gif)

FIG. 4 illustrates an alternative form of safety device which
is operable to make or break the connection between an
electrolytic hydrogen-oxygen cell (not shown in FIG. 4) and an
electric current source. The device comprises a cylindrical
container 40 in fluid communication with a liquid reservoir 41
via a passageway 42, and a quantity of mercury 42' contained in
the container and reservoir. Two electrodes 43 and 44 are
disposed one above the other in the container 40 and are
normally immersed in the mercury with a conductive path thereby
formed between them. The container is connected electrically in
series with an electrolytic cell (or cells) and in gaseous
communication therewith through a hose 45. An increase in gas
pressure resulting from generation of gases by the electrolytic
cell(s) causes the mercury to be displaced towards the reservoir
and the mercury level in the container 40 to fall. When the
pressure exceeds a predetermined level the mercury level falls
below that of the electrode 43 and electrical connection between
the two electrodes is broken. The electrical connection is again
restored when the gas pressure falls. A non-inflammable liquid,
such as silicone oil or freon is provided on top of the mercury
to ensure that any arc which may be generated between the
electrode 43 and the mercury is totally isolated from the gases
above the liquids.

![](5.gif)

FIG. 5 shows schematically an arrangement whereby an
exceedingly hot flame can be produced using the gaseous mixture
generated electrolytically by the apparatus previously
described. In this arrangement a mixture of hydrogen and oxygen,
preferably in stoichiometrical proportion, is passed via a line
50 between a pair of tungsten electrodes 51 to produce molecular
dissociation of the hydrogen and the oxygen and a very hot flame
52. It can be appreciated that whereas in an atomic hydrogen
flame a significant temperature rise is obtained by striking an
arc in the hydrogen, an even greater temperature rise can be
realized by striking the arc between the oxygen as well since
the dissociation energy of molecular oxygen is of the same order
of magnitude as that of molecular hydrogen.

![](6.gif)

FIG. 6 illustrates an arrangement for the magnetic separation
of oxygen from a mixture of oxygen and hydrogen, whereby the
oxygen can be used for flame cutting. The apparatus consists of
a chamber 60 containing a magnet 61 and is located in a conduit
62. A mixture of hydrogen and oxygen is passed through the
conduit and around the magnet 61. The diamagnetic oxygen is
diverted by the magnetic field into a transverse passageway 63
to a central conduit (not shown) leading from this passageway
and thence to a flame-cutting head. The paramagnetic hydrogen
continues along the conduit, past the magnet and can be allowed
to escape or can be collected, as desired. If the magnet is an
electromagnet it can be turned off when hydrogen and oxygen is
required as a mixture, and in that case the downstream side of
the conduit 62 can be closed off to prevent the loss of gas.

![](7.gif)

FIG. 7 illustrates a complete oxy-hydrogen generator and
welding apparatus comprising a gas generator 70, a current
regulating cell 71 and a power supply 72. The construction of
the electrodes 73 of the generator 70 and 74 of the cell 71 are
identical with those illustrated in FIGS. 2 and 3 respectively.
In this arrangement, however, the gas generator 70 and cell 71
are combined as an integrated unit and as such has some features
not found in the arrangements shown in FIGS. 2 and 3. In
particular the chamber 75 of the generator 70 and the chamber 76
of the current regulator cell 71 are separated by two partitions
77 and 78 defining between them a passageway communicating
between the two chambers. The respective electrodes of the cell
71 and a generator 70 are connected electrically in series with
the power supply.

Gas produced by electrolysis in the chamber 75 rises into the
space in the chamber above the electrodes 73, passes down the
passageway between the partitions 77 and 78, bubbles through the
electrolyte in the chamber 76 and thence passes through an
outlet opening 79 to a burner 80. An air trap reservoir 81 is
formed integrally with the cell 71 and is in liquid
communication therewith through an opening between the bottom of
the reservoir and the cell. When the pressure of the gas
generated by the generator 70 rises, this pressure causes the
electrolyte in the chamber 76 to be displaced into the reservoir
81 resulting in a reduction of the current being passed to the
generator 70 by the mechanism previously described in relation
to FIG. 3 of the drawings. In this way the cell 71 effectively
monitors the gas pressure and regulates the current to maintain
an approximately constant pressure. To ensure against the
possibility that the pressure should accidentally exceed a
predetermined maximum safe value, a spring-loaded safety
pressure valve 82 is provided at the top of the reservoir 81 to
release the excess pressure into the atmosphere.

The burner 80 is provided with a flash-back arrestor in the
form of a porous ceramic pellet 83 located in the gas flow path
between the handle part 84 of the burner and the burner tip 85.
The flash-back arrestor acts by quenching any flame blowing back
into the burner before the flame has a chance to reach the hose
86 connecting the burner with the gas generator.

The power supply is of the universal type, that is, it is
provided with a transformer 87 connectable to an alternating
current electrical supply and provided with a number of
electrical outlets for various purposes. One winding of the
transformer is connected to a bridge rectifier which provides
the d.c. current for the gas generator. Another winding is used
for arc welding or can be used to supply an arc for atomic
oxy-hydrogen welding. It will be appreciated that the
transformer is optional and that the generator can be connected
directly to the mains. In fact the bridge rectifier is not
essential either and can be omitted if desired.

In the operation of apparatus of the type described it is often
required to conveniently change between neutral and oxidizing
flames, for example when changing from a welding operation to a
cutting operation and the present invention makes provision for
the variation of these functions. Briefly, in accordance with
the present invention, apparatus for either oxy-hydrogen welding
or cutting may comprise a first electrolytic generator for
generating hydrogen and oxygen by the electrolysis of water in
substantially stoichiometric proportions to produce a neutral
flame and a further electrolytic generator from which hydrogen
and oxygen are separately delivered, which means for adding
either the hydrogen from this further cell, or the oxygen from
the further generator to the gas mixture obtained from the first
generator. This arrangement results in a most efficient
combination of functions when a neutral flame or other is
required. The hydrogen gas produced by the further generator,
when added to the flame mixture, burns with atmospheric oxygen
thereby producing a reducing flame. When an oxidizing flame is
required, the additional hydrogen is cut off and the oxygen
produced by the further generator is added to the flame mixture.
It will be appreciated that various designs can be employed for
either generator, for example, they may be completely
independent or they may share a common electrolyte. The further
gas generator can also, in practice, be made somewhat smaller
than the other generator since it does not have to produce the
bulk of the gas required.

It has been found that welding with hydrogen and oxygen in an
exact 2 to 1 ratio (as when the gases are produced
electrolytically) results in a particularly clean, oxide free
welded surface and a strong welded joint. For the same quality
welding to be produced by conventional gas welding technique
substantially greater skill is required and, in the case of
conventional hydrogen welding, for example, good welded joints
are obtained only with great difficulty due to the extreme
difficulty in obtaining and maintaining a neutral flame. With
the method of the present invention there is no difficulty in
obtaining a neutral flame, and hence the ease with which high
quality welds can be obtained.

Finally, it can sometimes be convenient to store hydrogen
and/or oxygen, generated electrolytically in a specially
designed container, or to slowly accumulate these gases and
then, when required, using the accumulated stored gas for extra
heavy work for a short time. It is quite hazardous to pressurize
a mixture of hydrogen and oxygen under very high pressures, of
course, but it is possible, in accordance with one aspect of the
invention, to store a useful amount of gas in a relatively small
volume at low pressures and this can be done by using a highly
gas absorbent metal in the storage container. The metal
palladium, for example, can absorb up to 900 times its own
volume of hydrogen and can be used with advantage for this
application. In fact useful amounts of hydrogen, for small scale
brazing work can readily be stored in a small hand held
container, containing a gas absorbent material.

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