U.S. patent number 3,851,146 [Application Number 05/289,483] was granted by the patent office on 1974-11-26 for apparatus for vapor generation.
This patent grant is currently assigned to The Dow Chemical Company. Invention is credited to Foster C. Bennett.
United States Patent |
3,851,146 |
Bennett |
November 26, 1974 |
APPARATUS FOR VAPOR GENERATION
Abstract
An apparatus for providing, in a continuous or intermittent
manner, a superheated vapor of an organic liquid, such as methylene
chloride, for reflowing plastic surfaces or causing a plastic
material to flow onto a surface to create a film or coating
thereon. The apparatus includes a tubular metal member defining a
flow passage for both the liquid and gaseous phases of the liquid
being vaporized. A vapor flow control member having a vapor flow
orifice is provided at one end of the tubular member while the
other end of the tubular member communicates with a source of
organic liquid under pressure through an on-off valve. A source of
electrical energy is connected in circuit with the tubular member
through a switch operated concurrently with the valve whereby
electrical current is caused to flow through the tubular member to
heat the member to a temperature adequate to vaporize the liquid
flowing therethrough. The tubular member is electrically and
thermally insulated by a shield and a handle associated with the
shield contains the valve and switch.
Inventors: |
Bennett; Foster C. (Columbus,
OH) |
Assignee: |
The Dow Chemical Company
(Midland, MI)
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Family
ID: |
26903081 |
Appl.
No.: |
05/289,483 |
Filed: |
September 15, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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208296 |
Dec 15, 1971 |
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Current U.S.
Class: |
392/397; 239/136;
392/478; 222/146.5; 392/476 |
Current CPC
Class: |
B05B
1/24 (20130101); F24H 1/00 (20130101) |
Current International
Class: |
B05B
1/24 (20060101); B05B 1/00 (20060101); F24H
1/00 (20060101); H05b 001/00 (); F22b 001/28 ();
B05b 001/24 () |
Field of
Search: |
;219/271-276,300,301,362,373,296-299 ;239/133,135,136,137,138
;222/146HE |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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482,715 |
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Apr 1938 |
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GB |
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13,070 |
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Jun 1933 |
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AU |
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Primary Examiner: Bartis; A.
Attorney, Agent or Firm: Baker; Glwynn R.
Parent Case Text
CROSS-REFERENCE TO RELATED APPLICATION
This application is a continuation-in-part of my copending
application filed Dec. 15, 1971, Ser. No. 208,296 now abandoned.
Claims
I claim:
1. An apparatus for converting a volatilizable organic liquid or
mixture of liquids into superheated vapors which consists
essentially of:
a tubular metal member which is electrically conductive but has a
resistance to the flow of an electrical current and which member
defines a flow path for the liquid to be vaporized and for the
vaporized liquid,
a vapor flow control member at one end of said tubular metal
member, said vapor control member having a vapor outlet orifice, a
manually actuated open-close liquid flow control member at the
opposite end of said tubular metal member for selectively
controlling liquid flow into said tubular metal member,
a source of electrical energy connected at a pair of spaced points
to said tubular metal member by means arranged to be controlled
concurrently with and in on-off corresponding relationship with
said liquid flow control member whereby electrical energy is caused
to flow through a predetermined segment of said tubular metal
member to heat the tubular metal member to a temperature to
vaporize the liquid flowing therethrough,
a source of volatilizable organic liquid connected in flow
communication with the tubular metal member through said liquid
flow control member, said source of liquid being under
superatmospheric pressure whereby the liquid therein is caused to
flow into the tubular metal member when the liquid flow control
member is opened,
the tubular metal member being heated to such a temperature and the
length of the heated portion of the tubular metal member, the bore
of the tubular metal member and the orifice of said vapor flow
control member being of such a size relative to each other such
that the liquid supplied under pressure into the tubular metal
member will vaporize and said vapor will be heated to above its
boiling point at a rate to maintain a pressure of vapor at the
vapor flow control member sufficient to propel the vapors from the
apparatus at least about one foot,
said means connecting said electrical energy source to said tubular
metal member including connectors in current flowing contact with
the respective ends of said tubular metal member,
said electrical energy source being connected in circuit with said
connectors and said connecting means further including a switch
associated with said liquid flow control member in concurrent
similarly functioning open-close relation to said liquid control
member for controlling application of energy to said connectors
from said source whereby electrical current is caused to flow
through the tubular member to heat the member to a temperature
adequate to vaporize the liquid flowing therethrough,
a connector connecting said tubular metal member through said
liquid flow control member to said source of vaporizable organic
liquid,
said tubular metal member, vapor flow member, and said liquid flow
control member being capable of withstanding superatmospheric
pressures and a temperature of 1,200.degree.F. and said electrical
energy connectors and switch being capable of withstanding five to
ten KVA alternating current power,
said tubular metal member electrically and thermally insulated by a
shield and a handle associated with said shield and containing the
liquid flow control member and the switch, said vapor control
member projecting from one end of the shield.
2. An apparatus for converting a volatilizable organic liquid or
mixture of liquids into superheated vapors which consists
essentially of:
a tubular metal member which is electrically conductive but has a
resistance to flow of an electrical current and which member
defines a flow passage for carrying both liquid and gaseous forms
of said liquid to be vaporized,
a vapor flow control member at one end of said tubular metal member
having a vapor outlet orifice,
a manually operated open-close liquid flow control member at the
other end of said tubular metal member for controlling liquid flow
into the tubular metal member,
said tubular metal member being disconnectable and removable from
said flow control member,
electrical energy connectors in current flowing contact with the
respective ends of said tubular metal member,
an electrical current source in circuit with said electrical energy
connectors and a switch associated with said liquid flow control
member in concurrent similarly functioning open-close relation to
said liquid control member for controlling application of energy to
said connectors from said source whereby electrical current is
caused to flow through the tubular member to heat the member to a
temperature adequate to vaporize the liquid flowing
therethrough,
a connector associating said tubular metal member through said
liquid flow control member to a source of vaporizable organic
liquid and means associated with the source for causing the liquid
to flow into the tubular metal member when the fluid control member
is opened,
said tubular metal member, vapor flow member, and said liquid flow
control member being capable of withstanding superatmospheric
pressures and a temperature of 1,200.degree.F. and said electrical
energy connectors and switch being capable of withstanding five to
ten KVA alternating current power,
said tubular metal member electrically and thermally insulated by a
shield and a handle associated with said shield and containing the
liquid flow control member and the switch, said vapor control
member projecting from one end of the shield.
Description
BRIEF DESCRIPTION OF THE INVENTION
The present invention relates to a novel apparatus and a process
employing the apparatus for vaporizing fluids, such as volatile
organic solvents or mixtures of solvents, to produce superheated
vapors of said fluid(s). More particularly, the present invention
concerns a pressurized apparatus from which superheated vapors of
volatile organic solvents, generated within the apparatus, can be
discharged in a controlled manner to impinge against a plastic
surface, e.g., coating or surface of a body of plastic, to
effectuate the modification of the surface, viz., remove surface
imperfections and defects, according to the vapor reflow principle
or to flow a plastic powder on a surface to create a film or
coating thereon.
Several embodiments of apparatus within the scope of the present
invention are illustrated in the Drawings:
FIG. 1 illustrates in cross-sectional elevation the configuration
of a light weight apparatus within the scope of the present
invention suitable for continuous or intermittent usage to produce
superheated vapors of a fluid, for example, a vaporizable organic
solvent or a mixture of vaporizable organic solvents and propel
them with sufficient force to effectively produce a pattern of
superheated vapors (vapors of the solvent or mixture of solvents
100.degree. to 300.degree.C. above their atmospheric boiling point)
up to 1 to 2 feet from the discharge orifice of the apparatus;
FIG. 2 illustrates another embodiment of a vaporizer element of the
present invention in cross-sectional view, which eliminates the
effect of inductance when alternating current is employed.
DETAILED DESCRIPTION OF THE INVENTION
In accordance with the present invention, having particular
reference to FIG. 1 of the Drawings, there is provided a tubular
member 10 which is made of a metal or an alloy of a metal having a
resistance sufficient to convert electrical energy, supplied at low
voltage and high amperage, into heat energy at a rate to supply,
within a length of several feet, the sensible heat necessary to
raise the temperature of the liquid to the boiling point, the heat
of vaporization of the liquid and the heat of superheat of the
vapor of the liquid to a predetermined temperature. Connected to
one end 11 of the tubular member 10 is an electric cable 12 which
provides one lead from the power source 13. Connected to the other
end 14 of the member 10 is another electric cable 15 which provides
the second lead from the power source 13, thus completing an
electric circuit from the power source 13 to the tubular member 10
(the electrical resistance) and back to the power source 13. In the
embodiment shown in FIG. 1, the tubular member 10 is provided with
a shielding member 16 which surrounds the member 10 and retains
insulation 17 in position to isolate member 10 from the shield,
thus insulating the member 10 from loss of heat to ambient
atmosphere, as well as electrically insulating the member 10 from
the ambient atmosphere and the operator. Extending from the
shielding member 16 is a handle member 18 to accommodate the manual
manipulation of the apparatus. The tubular member 10 is provided at
one end 11 with a nozzle or orifice 19 or other vapor pattern
directing means. The other end 14 of tubing 10 is provided with a
tubular electrical and heat insulating connector 20. Connector 20
is further connected by piping or flexible tubing 21 to a
pressurized container 22 which contains the liquid to be vaporized.
Pressure controls and a source of pressure, neither of which are
shown, are associated with the container 22. The power source 13 is
also provided with controls, transformers, and/or rectifiers, etc.,
as necessary to produce the desired voltage and current to provide
the wattage to produce the desired temperature in the member
10.
The tubular member 10 is preferably provided, as shown, with a
fluid flow control valve 23 to permit adjustment of the rate of
flow and a simultaneously operable trigger mechanism or valve 24 to
permit off-on flow of fluid through tube 10 as well as an
electrical switch which simultaneously permits flow of electricity
to the member 10 when fluid is flowing and shuts off the flow of
electricity to the member 10 when fluid flow is interrupted.
In operation of the apparatus illustrated in FIG. 1, a
volatilizable liquid, for example, a halogenated hydrocarbon such
as methylene chloride, is provided in container 22 and the
container pressurized with from about 30 to about 200 pounds per
square inch air pressure. The power source is activated, and, for
example, if methylene chloride is to be delivered under 30-35 psig.
as a superheated vapor at 400.degree.F. just outside the nozzle 19,
is adjusted to deliver about 30 volts at 75 amperes of alternating
current, converted from 220 volt source through an isolated
secondary of a transformer. Thermocouples, as at points x and y or
by trial and error, simplify the adjustment of the power source to
provide a superheated vapor of methylene chloride of a temperature
of about 400.degree.F.; it being clearly understood the temperature
of the vapor inside the apparatus will necessarily be higher than
that outside the nozzle due to expansion and cooling phenomena of
gases. The apparatus illustrated in FIG. 1 is capable of delivering
several gallons an hour of such vapor continuously or
intermittently. The preferred embodiment of the apparatus
illustrated in FIG. 1 includes the control of the temperature of
the member 10 by using the signal generated by the thermocouples x
and y to either shut off the current or turn it on
intermittently.
It is one advantage of the apparatus of the present invention that
once the current is turned off and simultaneously the flow of fluid
is stopped, the member 10 cools rapidly since it is of
inconsequential volume, that is, its volume as a heat sink is less
than the volume of the liquid in the tube. The apparatus can be
even more rapidly cooled by merely allowing a small quantity of
liquid from the container 22 to pass through the member 10 after
the current has been shut off at the transformer controls, for
example. Similarly, the member 10 heats up rapidly. Both of these
features are important when the liquid being heated is degradable
by prolonged contact with high temperature.
The embodiment of the present invention illustrated in FIG. 2
illustrates one method for winding the tubular heating member to
eliminate substantially the effect of inductance associated with a
current flowing through a coil. The tubular member 210 is wound
back over itself so that the current flowing at any instant in the
inner coil 210A is directly opposite that flowing in the 210B. The
outlet end 211 is provided with a nozzel 219 and opposite ends of
the coil 210, i.e., 211 and 214, are provided with electrical
connection 212 and 215 which are connected to a power source, not
shown. Similarly, the coil 210 is connected at end 214 to a source
of liquid not shown. The apparatus may be, in all other aspects,
identical with that illustrated in FIG. 1, that is, the coil may be
arranged within a shell provided with a handle to form a manually
operated apparatus.
It is to be understood that either configuration of the coil 10 or
210 of FIGS. 1 and 2, respectively, may be employed to heat or
vaporize liquid materials for purposes other than those
contemplated by the gun-like design. Thus, one could employ the
coil to heat water or to generate saturated or superheated steam.
Similarly, the coil may be employed to heat liquids or generate
vapors for chemical reactions.
Having described my invention in general, the following examples
are set forth to illustrate specific embodiments of the
invention.
EXAMPLE 1
A type 316 stainless steel tube having an outside diameter of 1/4
inch and a wall thickness of 0.028 inch was close wound on a 2 inch
mandrel to provide thirteen turns then a space equal to about two
turns followed by fourteen turns. The coil was started by bringing
a point about five inches from one end into a groove in the mandrel
near its center, and bringing the tubing to the rear of the mandrel
along a groove to the point of beginning of the coil forming
section. The coil so wound was insulated between each turn with a
disc of insulating material, compressed asbestos, capable of
withstanding 1,200.degree.F. temperatures. The coil was also
insulated along and about its peripheral dimensions with an
alumina-silica ceramic fiber insulation (e.g., Fiberfrax or
Kaowool) of about 1/4 inch. A 31/4 inch OD tube of Type 304
stainless steel was placed about the assembly, closed at the
rearward end and provided with an end cap to receive the discharge
end of the tube and aid in holding the tube within the shield
assembly. The shield was provided with a handle of metal to
surround the inlet end of the tube. The space between the tube and
the handle was insulated. The inlet end of the tube was provided
with a fitting to receive a Teflon nipple, to which was fitted a
liquid control valve. The leads from a 10 KVA alternating current
isolated secondary 220 volt transformer were brazed, one to the
tube and one to the handle. A container provided with an air
pressure system was connected to the control valve. Upon
pressurization of the container which contained methylene chloride,
and activation of the transformer to deliver 30 volts and 75
amperes, the methylene chloride flowing into the tube was converted
into a vapor which had a temperature upon leaving the nozzle of
about 400.degree.F.
The following table illustrates the versatility of the apparatus of
FIG. 1 to vaporize various requirements of a methylene chloride
composition employed to flow an acrylic paint surface.
______________________________________ Flow Rate Watts at Indicated
Gallons/Hour Ave. Voltage ______________________________________ 1
600/16.5 2 1200/22 3 1800/27.5 4 2400/33 5 3000/38.5 6 3600/44 7
4200/49.5 ______________________________________
The pressure on the apparatus provided a pattern of vapor of about
1 square foot one foot from the nozzle which upon impinging on the
surface of a panel coated with an acrylic lacquer of the type used
to paint automobiles and which painted panel had been lightly
sanded, removed surface imperfections.
The apparatus illustrated in FIG. 1 can also be operated from a
110V source using a five KVA transformer -- 32 volts isolated
secondary to supply up to 2 gallons per hour of the methylene
chloride composition at 400.degree.F.
* * * * *