CN2246151Y - Gas preparing and feeding pot - Google Patents
Gas preparing and feeding pot Download PDFInfo
- Publication number
- CN2246151Y CN2246151Y CN 96202737 CN96202737U CN2246151Y CN 2246151 Y CN2246151 Y CN 2246151Y CN 96202737 CN96202737 CN 96202737 CN 96202737 U CN96202737 U CN 96202737U CN 2246151 Y CN2246151 Y CN 2246151Y
- Authority
- CN
- China
- Prior art keywords
- vaporizer
- main
- inlet pipe
- liquid
- tank body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The utility model relates to a gas preparing and supply pot which is characterized in that a pot body is in a double-layer structure, a pair of gasifying chambers are arranged in a main gasifying chamber, and a liquid inlet pipe and a liquid level control device is arranged between the two gasifying chambers; the lower end of an air inlet pipe which is positioned in the auxiliary gasifying chamber is positioned at the bottom of the auxiliary gasifying chamber, and the upper end is communicated with the upper part of the main gasifying chamber. Permanent magnetic materials are installed on the lower part of the main gasifying chamber, the upper part and the lower part of the main gasifying chamber are communicated with a liquid storage pot respectively by a gas equilibrium pipe and a liquid delivery pipe. An interlayer of the double-layer pot body is communicated with an outer thermal source through a heat supply pipe and a heat return pipe; a gasification supporting pipe directly extends into the bottom of the main gasifying chamber. The gas preparing and supply pot has the advantages of simple structure, high gasifying rate of oil liquid in pot, low cost and fabricating cost.
Description
The utility model relates to a kind of gas-fired equipment, relates in particular to a kind of gas producing and supply jar.
At present in petrochemical industry, oil field, refinery ethylene project etc. be by-product fluid all, have because of stock discard in vain, as the oil field facing to sky incendiary sky lamp, constantly all wasting precious resources, these byproduct fluid whole nations all have up to ten million tons to wait for processing treatment every year.Several necessarily having succeeded in developing first in Jiangsu Province of Shanghai relevant energy development department investment utilizes petrochemical industry byproduct fluid to be processed into industry or domestic fuel through special, but produces the heavy 1.5 ten thousand tons of scales that only have per year.Therefore some patent introduction utilizes the petrochemical industry by-product oil to carry out the catalytic pyrolysis gas combustion apparatus night, some additives of increase in device that have, but the most body of this class device is huge, complex structure, easy-maintaining not, the chemical industry additive that is increased mostly has certain side effect, and all be unable to do without electric heater unit, not only waste energy, also strengthened production cost.
A kind of gas producing and supply jar that is applicable to flammable fluid that the purpose of this utility model designs at existing weak point in the above-mentioned prior art just, this system is simple for jar structure, jar inner fluid vaporization rate height, installation and maintenance are convenient, in roof, the building, ground all can install.
The purpose of this utility model realizes by following measure: this gas producing and supply jar comprises tank body, main vaporizer and be arranged on vaporizer and outer pipeline between communicating pipe, wherein: tank body is a bilayer structure, be provided with a secondary vaporizer in the main vaporizer, be provided with a liquid-inlet pipe and fluid level control device between two vaporizers, its lower end of inlet pipe that is arranged in secondary vaporizer is in secondary vaporizer bottom, the upper end communicates with main vaporizer top, bottom at main vaporizer is equipped with permanent magnet material, the upper and lower of main vaporizer communicates with receiver by gas-liquid equilibrium pipe and tubing respectively, the interlayer of double-deck tank body communicates with outer thermal source by heating tube and product heat cal rod, helps tracheae to pass the bottom that double-deck tank body directly extend into main vaporizer.
In the utility model, fluid level control device by liquid-inlet pipe, be installed on the pull bar in the liquid-inlet pipe and be connected pull bar that up and down the ball float and the valve at two ends are formed; Be evenly equipped with a plurality of gasification boards on the inwall of tank body, the gasification board surface is through the steel sand shot peening, and its effect is to strengthen the fluid surface-area, quickens the fluid gasification; Permanent magnet material in main vaporizer bottom is a dozens of ball-point pen type magnet, with its with a silicon bronze wire harness wear string together in ring, be fixed on secondary vaporizer bottom surface with magnetic conductive metal not then, its principle be magnetic bead and silicon bronze wire harness physics and chemistry phenomenon and produce certain magnetic field around fluid tinyization of molecular grouping and on spray nozzle of gas kitchen ranges, be difficult for coking behind gasification and the air thorough mixing easily; The tracheae outlet that helps that extend into main vaporizer bottom is bell mouth shape; The interlayer of double-deck tank body communicates with solar water heater by heating tube and product heat cal rod; The inlet pipe that is arranged in secondary vaporizer is two, is symmetrically distributed in the secondary vaporizer.
The utility model has following advantage compared to existing technology: because this system gas tank is to utilize petrochemical industry byproduct system for combustion gas, have great significance aspect energy-conservation developing.Also be provided with the various gasification installations that quicken in this body, vaporization rate height not only, and do not use any additives to make and confess nonpoisonous and tasteless qualified combustion gas; Then, this system for jar heating by the solar energy converting heating unit for charged heating unit, cost is minimized, have energy-saving effect.This system is little, in light weight for tank volume, and complete machine is made up of various in addition parts, can determine that its volume is big or small according to gas consumption and assemble; The dismounting of this machine is easy to maintenance, and ground all can be installed in roof, the building, and can endure that feed channel, gas pipe are advanced, liquefied gas pipeline networks a kind of industrial or civilian gas producing and supply machine that is suitable for preferably of can yet be regarded as with the sky.
The drawing of accompanying drawing is described as follows:
Fig. 1 is a structural front view of the present utility model.
Fig. 2 is the A-A sectional view of Fig. 1.
Fig. 3 is the structural representation that the utility model links to each other with solar water heater and storage liquid bag.
The utility model is explained in detail below in conjunction with accompanying drawing:
As Fig. 1, Fig. 2, shown in Figure 3: this gas producing and supply jar comprise tank body (1), be arranged in the main vaporizer (2) of jar and be arranged on vaporizer and outer pipeline between communicating pipe (3), wherein: tank body is a double-layer heat insulation cover pack arrangement, on the inwall of tank body, be evenly equipped with a plurality of gasification boards (4), the gasification board surface is through the steel sand shot peening, its effect is to strengthen the fluid surface-area, quickens the fluid gasification; Be provided with a secondary vaporizer (5) in the main vaporizer (2), be provided with a liquid-inlet pipe (6) and fluid level control device between two vaporizers, fluid level control device by liquid-inlet pipe (6), be installed on the pull bar (7) in the liquid-inlet pipe and be connected pull bar that up and down the ball float (8) and the valve (9) at two ends are formed; Two inlet pipe (10) that are arranged in secondary vaporizer (5) are symmetrically distributed in secondary vaporizer, the lower end of inlet pipe is in secondary vaporizer bottom, the upper end communicates with main vaporizer (2) top, in the bottom of main vaporizer (2) permanent magnet material (11) is installed, permanent magnet material is for imitating ten ball-point pen type magnet, it is worn to string together with a silicon bronze wire harness (12) be ring, endure the back and be fixed on secondary vaporizer (5) bottom surface with magnetic conductive metal not, its principle be magnetic bead and silicon bronze wire harness physics and chemistry phenomenon and produce certain magnetic field around fluid tinyization of molecular grouping and on spray nozzle of gas kitchen ranges, be difficult for coking behind gasification and the air thorough mixing easily; The upper and lower of main vaporizer (2) communicates with receiver (15) by gas-liquid equilibrium pipe (13) and tubing (14) respectively, the interlayer of double-deck tank body communicates with apparatus for heating water by solar energy (18) by heating tube (16) and product heat cal rod (17), help tracheae (19) to pass the bottom that double-deck tank body directly extend into main vaporizer (2), bell mouth shape in its outlet, the hot gas that is connected with in its pipe after the solar energy equipment heating blows main vaporizer bottom surface, quickens the fluid gasification.The consumption of water is supplied with by the water level replenisher in the solar water heater.
Be described below below in conjunction with the working process and the principle of accompanying drawing this machine: solar heat collector with the heating of the water in its insulation bag make it to expand the system that flows into for jar laminated heat-preserving cover bag in, utilize conduction of heat to make the fluid temperature influence in the main vaporizer and molecular motion is quickened to lay the first stone for combustion gas for system.Be located at fluid level control device between major and minor two vaporizers by liquid-inlet pipe, be installed on the pull bar in the liquid-inlet pipe and be connected pull bar that up and down the ball float and the valve at two ends are formed, its principle of work be when fluid when liquid-inlet pipe enters secondary vaporizer, along with oil level increases and ball float come-up and pulling pull bar, when oil level slowly is increased to certain altitude, thereby the valve of pull bar lower end is promptly closed oil inlet pipe and is reached the purpose that oil level is controlled automatically.That gives main vaporizer air feed helps that gas is to spray from the flaring exit shower nozzle through compressor pressurizes and solar energy equipment heating back in the tracheae, blow by magnetic field magnetisation and molecular grouping has become tiny fluid boiling, make fluid accelerated motion by force, the intermolecular fission that runs foul of each other, reach the part oil molecule and climb away the formation gasification of fluid surface, and from two inlet pipe, feed in the fluid of secondary vaporizer bottom, stir once more make the fluid ebullition, gasification enter secondary vaporizer top communicate with outer pipeline enter user's pipe network communicating pipe.Utilize the gas-liquid equilibrium pipe for the storage liquid bag of jar fuel feeding liquid again by high potential difference and communicate for this system and can make transition pipeline in time replenish fluid in the main vaporizer with main vaporizer.
The utility model also can not use heating unit, and tank body itself also is a single layer structure, and other structure in jar and connection are all identical with accompanying drawing 1.
Claims (7)
1, the utility model relates to a kind of gas producing and supply jar, it comprises tank body (1), main vaporizer (2) and be arranged on vaporizer and outer pipeline between communicating pipe (3), it is characterized in that: tank body (1) is a bilayer structure, be provided with a secondary vaporizer (5) in the main vaporizer (2), be provided with a liquid-inlet pipe (6) and fluid level control device between two vaporizers, its lower end of inlet pipe (10) that is arranged in secondary vaporizer (5) is in secondary vaporizer bottom, the upper end communicates with main vaporizer (2) top, in the bottom of main vaporizer (2) permanent magnet material (11) is installed, the upper and lower of main vaporizer communicates with receiver (15) by gas-liquid equilibrium pipe (13) and tubing (14) respectively, the interlayer of double-deck tank body communicates with outer thermal source by heating tube (16) and product heat cal rod (17), helps tracheae (19) to pass the bottom that double-deck tank body directly extend into main vaporizer (2).
2, gas producing and supply jar according to claim 1 is characterized in that: fluid level control device by liquid-inlet pipe (6), be installed on the pull bar (7) in the liquid-inlet pipe and be connected pull bar that up and down the ball float (8) and the valve (9) at two ends are formed.
3, gas producing and supply jar according to claim 1 is characterized in that: be evenly equipped with a plurality of gasification boards (4) on the inwall of tank body (1).
4, gas producing and supply jar according to claim 1, it is characterized in that: the permanent magnet material (11) in main vaporizer (2) bottom is a dozens of ball-point pen type magnet, with its with a silicon bronze wire harness (12) wear string together in ring, be fixed on secondary vaporizer (5) bottom surface with magnetic conductive metal not then.
5, gas producing and supply jar according to claim 1 is characterized in that: tracheae (19) outlet that helps that extend into main vaporizer (2) bottom is bell mouth shape.
6, gas producing and supply jar according to claim 1 is characterized in that: the interlayer of double-deck tank body communicates with solar water heater (18) by heating tube (16) and product heat cal rod (17).
7, gas producing and supply jar according to claim 1 is characterized in that: the inlet pipe (10) that is arranged in secondary vaporizer (5) is two, is symmetrically distributed in the secondary vaporizer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 96202737 CN2246151Y (en) | 1996-01-23 | 1996-01-23 | Gas preparing and feeding pot |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 96202737 CN2246151Y (en) | 1996-01-23 | 1996-01-23 | Gas preparing and feeding pot |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2246151Y true CN2246151Y (en) | 1997-01-29 |
Family
ID=33888569
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 96202737 Expired - Fee Related CN2246151Y (en) | 1996-01-23 | 1996-01-23 | Gas preparing and feeding pot |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2246151Y (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103409186A (en) * | 2013-07-17 | 2013-11-27 | 张家港保税区巨能天成国际贸易有限公司 | Pentane oil-making-gas gasifier |
CN107588431A (en) * | 2017-09-06 | 2018-01-16 | 巨烃新能源技术有限公司 | A kind of superconducting fluid heated type combustion gas process system |
CN109847686A (en) * | 2019-03-28 | 2019-06-07 | 万荣金坦能源科技有限公司 | A kind of liquid fuel extruding fission system and fission method freezed |
-
1996
- 1996-01-23 CN CN 96202737 patent/CN2246151Y/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103409186A (en) * | 2013-07-17 | 2013-11-27 | 张家港保税区巨能天成国际贸易有限公司 | Pentane oil-making-gas gasifier |
CN107588431A (en) * | 2017-09-06 | 2018-01-16 | 巨烃新能源技术有限公司 | A kind of superconducting fluid heated type combustion gas process system |
CN107588431B (en) * | 2017-09-06 | 2019-12-06 | 巨烃新能源技术有限公司 | superconducting liquid heating type gas process system |
CN109847686A (en) * | 2019-03-28 | 2019-06-07 | 万荣金坦能源科技有限公司 | A kind of liquid fuel extruding fission system and fission method freezed |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN215085877U (en) | Gas-liquid separation integrated device in hydrogen production system | |
CN2246151Y (en) | Gas preparing and feeding pot | |
CN108358168A (en) | A kind of bromine high efficiency extraction system | |
CN208916818U (en) | A kind of iron powder hydrogen production reaction furnace and device | |
CN110950303A (en) | Titanium alloy methanol-water reformer and hydrogen production equipment | |
CN105907481A (en) | Alternating serial reaction device for producing biodiesel from high-pressure gas-phase methanol | |
CN101403471A (en) | Liquid gas gasification method and its circulation type gasification apparatus | |
KR200459027Y1 (en) | Negative-pressure type coal gas generating equipment | |
CN103818976B (en) | Direct-fired method for spraying and desalting and device | |
CN203162911U (en) | Phase change heating heat machine | |
CN2422543Y (en) | Light hydrocarbon liquid fuel vaporising device | |
CN207377678U (en) | A kind of schizolysis hydrogen production plant and automobile | |
CN112808192A (en) | Heat recoverable high-efficient phosphorus trichloride apparatus for producing | |
CN204554804U (en) | A kind of seawater decomposition combustion device | |
WO1994023188A1 (en) | A device and a method for automobile self-producing hydrogen fuel | |
CN205137404U (en) | Energy -efficient full -automatic gas vapor generation stove | |
CN217844821U (en) | Coal industry cooling device | |
CN103965967A (en) | Hydrogen-rich gas production equipment as well as hydrogen-rich gas production process and solar condensation heat collecting coal gasifier | |
CN210035447U (en) | Device for heating hot water by steam circulation | |
CN212108338U (en) | Energy-concerving and environment-protective type steam generator | |
CN217154545U (en) | Photovoltaic heating circulating pipe water tank | |
CN220793099U (en) | Electromagnetic steam generator without water storage | |
CN113955714B (en) | Magnesium hydride hydrolysis controllable hydrogen system, method and application | |
CN102628587B (en) | Phase change heating heat machine and heating method by using phase change heating heat machine | |
CN202598621U (en) | Commercial fusel oil high-flame oven |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |