CN106705023A - Water-electricity heat exchange high-pressure steam circulating method - Google Patents
Water-electricity heat exchange high-pressure steam circulating method Download PDFInfo
- Publication number
- CN106705023A CN106705023A CN201510793788.0A CN201510793788A CN106705023A CN 106705023 A CN106705023 A CN 106705023A CN 201510793788 A CN201510793788 A CN 201510793788A CN 106705023 A CN106705023 A CN 106705023A
- Authority
- CN
- China
- Prior art keywords
- housing
- gas
- separation chamber
- liquid
- heat
- 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.)
- Pending
Links
Landscapes
- Control For Baths (AREA)
Abstract
The invention discloses a water-electricity heat exchange high-pressure steam circulating method. A sealed shell with the hollow interior is included. A heat exchange pipe is arranged in the shell. The bottom end of a gas-liquid separation chamber is arranged in the shell. The gas-liquid separation chamber is arranged in a coiled structure formed by the heat exchange pipe. A gas outlet pipe is arranged at the top end of the gas-liquid separation chamber and provided with a pressure gauge, a safety valve and a pressure regulator. A water bath is arranged in the shell, and the water bath is connected with an electric heater. A thermocouple is arranged in the coiled structure formed by the heat exchange pipe. An electrical control box and a junction box are arranged on the outer portion of the shell. A liquid level sensor and a temperature sensor are arranged in the shell and both connected with the electrical control box. A dirt discharge plate is arranged in the shell, and a water drainage pipe is arranged in the center of the dirt discharge plate. The mechanism structure is simple, the heating and gasifying process can be integrally controlled, manpower and material resources are saved, control is accurate, and the inner state can be fed back in time.
Description
Technical field
The present invention relates to a kind of mechanism, more particularly, to a kind of high steam round-robin method of water power heat exchange.
Background technology
Electrical heating is at present to metal material efficiency of heating surface highest, fastest, the induction heating equipment of low-loss and energy-saving environment-friendly type.Electrical heating, also known as high frequency heating machine, HF induction heating apparatus, high-frequency induction heating apparatus, high-frequency heating power, high frequency electric source, high frequency furnace.High-frequency welder, high frequency sensing heating machine, high frequency sensing heater (soldering apparatus) etc., in addition also Intermediate Frequency Induction Heating Equipment, superelevation frequency induction heating equipment etc..Range of application is quite varied.Heat energy is converted electric energy into heat object.It is a kind of form of utilization of power.Compared with general fuel is heated, electrical heating can obtain higher temperature (such as electric arc heated, temperature is up to more than 3000 DEG C), it is easy to accomplish temperature is automatically controlled and far distance controlled, vehicle-mounted electric-heating cup.Heating object can be on demand set to keep certain Temperature Distribution.Electrical heating can inside heating object direct heat, thus the thermal efficiency is high, and programming rate is fast, and can according to the technological requirement of heating, realize overall uniform heating or it is local plus（Including surface heating）, easily realize heating in vacuum and control atmosphere heating.During electrical heating, the waste gas of generation, residue and flue dust are few, can keep the cleaning of heating object, free from environmental pollution.Therefore, electrical heating is widely used in the fields such as production, scientific research and experiment.The aspects such as manufacture, machine components and surface hardening, the melting of ferroalloy and the manufacture of Delanium particularly in monocrystalline and transistor, all using Electric heating.According to the difference of electric energy conversion regime, electrical heating is generally divided into resistance heating, sensing heating, electric arc heated, electron beam heating, infrared heating and medium heating etc..The complex structure of existing electric heating gasification structure, and transformation efficiency is low during heating and gasifying, wastes the energy, it is impossible to meet factory needing.
The content of the invention
Complex structure it is an object of the invention to overcome above-mentioned existing electric heating gasification structure, and transformation efficiency is low during heating and gasifying, control process is cumbersome, need to consume substantial amounts of human resources, for the problem that internal state can not be fed back in time, devise a kind of high steam round-robin method of water power heat exchange, the simple structure of the mechanism, integrated heating and gasifying process can be controlled, save manpower and materials, and control is accurate, and can be fed back in time for internal state, solve the complex structure of existing electric heating gasification structure, and transformation efficiency is low during heating and gasifying, control process is cumbersome, need to consume substantial amounts of human resources, for the problem that internal state can not be fed back in time.
The purpose of the present invention is achieved through the following technical solutions：A kind of high steam round-robin method of water power heat exchange, seal casinghousing including inner hollow, heat-exchange tube is provided with the housing, heat-exchange tube is bent into disk-like structure, one end of heat-exchange tube is arranged on hull outside through housing, the other end is communicated with gas-liquid separation chamber, the bottom of gas-liquid separation chamber is set in the housing, gas-liquid separation chamber is arranged in the disk-like structure of heat-exchange tube formation, the top of gas-liquid separation chamber is provided with escaping pipe, escaping pipe one end connects with the top of gas-liquid separation chamber, the other end is arranged on the outside of housing, escaping pipe is arranged on and pressure gauge is provided with one end of hull outside, safety valve and pressure regulator, safety valve is arranged between pressure gauge and pressure regulator, pressure gauge is arranged between safety valve and gas-liquid separation chamber；Water bath is provided with the housing, water bath is arranged on the lower section of gas-liquid separation chamber, and water bath is connected with electric heater, and electric heater is arranged on hull outside and is fixed on the outer wall of housing；Thermocouple is provided with the disk-like structure that the heat-exchange tube is formed, the bottom insertion of thermocouple is in the housing；The hull outside is provided with electric control box and terminal box, and electric control box and terminal box are connected with each other, electric control box and with electric heater connection, thermocouple and pressure regulator are connected with electric control box；The enclosure interior is provided with liquid level sensor and temperature sensor, and liquid level sensor and temperature sensor are connected with electric control box；The enclosure interior is provided with blowdown plate, housing is divided into two sealed chambers by blowdown plate, blowdown plate is arranged on the lower section of gas-liquid separation chamber, heat-exchange tube and water bath, the top surface of blowdown plate is recessed towards housing bottom surface, the center of blowdown plate is provided with drainpipe, drainpipe one end connects through blowdown plate with enclosure interior, and the other end is arranged on hull outside through housing.
Overflow pipe is provided with the housing, overflow pipe is connected with enclosure interior, and one end that overflow pipe is connected with enclosure interior is near the top of housing.
Water level controller is provided with the housing, heat-exchange tube is arranged on one end of hull outside and is provided with liquid inlet electromagnetic valve and liquid filtration device, and liquid inlet electromagnetic valve, thermocouple and water level controller are connected with terminal box.
Blow-off pipe is provided with the gas-liquid separation chamber, one end of blow-off pipe is arranged on hull outside.
In sum, the beneficial effects of the invention are as follows：The simple structure of the mechanism, integrated heating and gasifying process can be controlled, save manpower and materials, and control is accurate, and can in time be fed back for internal state, solve the complex structure of existing electric heating gasification structure, and transformation efficiency is low during heating and gasifying, control process is cumbersome, it is necessary to consume substantial amounts of human resources, for the problem that internal state can not be fed back in time.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Mark and corresponding parts title in accompanying drawing：1-liquid filtration device；2-liquid inlet electromagnetic valve；3-thermocouple；4-pressure gauge；5-safety valve；6-pressure regulator；7-electric control box；8-terminal box；9-water level controller；10-blow-off pipe；11-electric heater；12-overflow pipe；13-drainpipe；14-housing；15-water bath；16-blowdown plate；17-gas-liquid separation chamber；18-heat-exchange tube；19-liquid level sensor；20-temperature sensor；21-escaping pipe.
Specific embodiment
With reference to embodiment and accompanying drawing, the present invention is described in further detail, but embodiments of the present invention are not limited only to this.
Embodiment：
As shown in Figure 1,A kind of high steam round-robin method of water power heat exchange,Seal casinghousing 14 including inner hollow,Heat-exchange tube 18 is provided with the housing 14,Heat-exchange tube 18 is bent into disk-like structure,One end of heat-exchange tube 18 is arranged on outside housing 14 through housing 14,The other end is communicated with gas-liquid separation chamber 17,The bottom of gas-liquid separation chamber 17 is arranged in housing 14,Gas-liquid separation chamber 17 is arranged in the disk-like structure of the formation of heat-exchange tube 18,The top of gas-liquid separation chamber 17 is provided with escaping pipe 21,The one end of escaping pipe 21 connects with the top of gas-liquid separation chamber 17,The other end is arranged on the outside of housing 14,Escaping pipe 21 is arranged on and pressure gauge 4 is provided with the one end outside housing 14,Safety valve 5 and pressure regulator 6,Safety valve 5 is arranged between pressure gauge 4 and pressure regulator 6,Pressure gauge 4 is arranged between safety valve 5 and gas-liquid separation chamber 17；Water bath 15 is provided with the housing 14, water bath 15 is arranged on the lower section of gas-liquid separation chamber 17, and water bath 15 is connected with electric heater 11, and electric heater 11 is arranged on the outside of housing 14 and is fixed on the outer wall of housing 14；Thermocouple 3 is provided with the disk-like structure that the heat-exchange tube 18 is formed, the bottom of thermocouple 3 is inserted in housing 14；Electric control box 7 and terminal box 8 are provided with outside the housing 14, and electric control box 7 and terminal box 8 are connected with each other, electric control box 7 and are connected with electric heater 11, thermocouple 3 and pressure regulator 6 are connected with electric control box 7；The housing 14 is internally provided with liquid level sensor 19 and temperature sensor 20, and liquid level sensor 19 and temperature sensor 20 are connected with electric control box 7；The housing 14 is internally provided with blowdown plate 16,14 points by housing of blowdown plate 16 is two sealed chambers, blowdown plate 16 is arranged on the lower section of gas-liquid separation chamber 17, heat-exchange tube 18 and water bath 15, the top surface of blowdown plate 16 is recessed towards the bottom surface of housing 14, the center of blowdown plate 16 is provided with drainpipe 13, the one end of drainpipe 13 is connected through blowdown plate 16 with the inside of housing 14, and the other end is arranged on outside housing 14 through housing 14；Overflow pipe 12 is provided with the housing 14, overflow pipe 12 is connected with the inside of housing 14, and one end that overflow pipe 12 is connected with the inside of housing 14 is near the top of housing 14；Water level controller 9 is provided with the housing 14, heat-exchange tube 18 is arranged on the one end outside housing 14 and is provided with liquid inlet electromagnetic valve 2 and liquid filtration device 1, and liquid inlet electromagnetic valve 2, thermocouple 3 and water level controller 9 are connected with terminal box 8；Blow-off pipe 10 is provided with the gas-liquid separation chamber 17, one end of blow-off pipe 10 is arranged on outside housing 14.In the technical program, electric control box 7 and terminal box 8 are all existing structures, heating and gasifying process is controlled by them, convenient operation, security is improved simultaneously, before the heat-exchange tube 18 that liquid enters in housing 14, filtered by liquid filtration device 1, impurity treatment therein is clean, after liquid inlet electromagnetic valve 2 experiences liquid to be entered, just signal is transported in terminal box 8, so that the control anti-explosion electric heater 11 of electric control box 7 and thermocouple 3 proceed by heating, heat-exchange tube 18 swaps heat, so that liquid gasification, substantially increase operating efficiency, reduce the middle stand-by period.Liquid after gasification is separated in gas-liquid separation chamber 17, gas is transported to the place of needs by escaping pipe 21, during gas transmission out, it is adjusted for the atmospheric pressure value that escaping pipe 21 is exported by safety valve 5 and pressure regulator 6, so that reaching rational numerical value, subsequent use can directly be carried out, shorten pilot process, after after work for a period of time, when cleaning is needed in gas-liquid separation chamber 17, sewage treatment is carried out by blow-off pipe 10, and the water in housing 14 is then discharged by drainpipe 13, due to the accumulation of impurity, drainpipe 13 cannot discharge sewage, easily cause accumulation, specially there is provided the recessed blowdown plate 16 of top surface, in sewage being imported into drainpipe 13 in cleaning, so that being cleaned inside housing 14.Overflow pipe 12 be prevent water level in housing 14 too it is high cause internal pressure excessive and design water is discharged, limit its peak level, liquid level sensor 19 and temperature sensor 20 are that liquid level and temperature are monitored, the numerical value that will be detected is timely fed back in electric control box 7, it is adjusted according to numerical value set in advance, ensure the liquid level in housing 14 with temperature in rational scope, what is gasified is in hgher efficiency, overall-in-one control schema is realized simultaneously, inconvenience and error rate that single step is brought by artificial operation is reduced.
The simple structure of the mechanism, integrated heating and gasifying process can be controlled, save manpower and materials, and control is accurate, and can in time be fed back for internal state, solve the complex structure of existing electric heating gasification structure, and transformation efficiency is low during heating and gasifying, control process is cumbersome, it is necessary to consume substantial amounts of human resources, for the problem that internal state can not be fed back in time.
The above; only it is presently preferred embodiments of the present invention; any formal limitation is not done to the present invention, every any simple modification, equivalent variations substantially made to above example according to technology of the invention, method are each fallen within protection scope of the present invention.
Claims (4)
1. the high steam round-robin method that a kind of water power exchanges heat, it is characterised in that：Seal casinghousing including inner hollow（14）, the housing（14）In be provided with heat-exchange tube（18）, heat-exchange tube（18）It is bent into disk-like structure, heat-exchange tube（18）One end pass through housing（14）It is arranged on housing（14）Outside, the other end is communicated with gas-liquid separation chamber（17）, gas-liquid separation chamber（17）Bottom be arranged on housing（14）In, gas-liquid separation chamber（17）It is arranged on heat-exchange tube（18）In the disk-like structure of formation, gas-liquid separation chamber（17）Top be provided with escaping pipe（21）, escaping pipe（21）One end and gas-liquid separation chamber（17）Top connection, the other end is arranged on housing（14）Outside, escaping pipe（21）It is arranged on housing（14）Pressure gauge is provided with outside one end（4）, safety valve（5）And pressure regulator（6）, safety valve（5）It is arranged on pressure gauge（4）And pressure regulator（6）Between, pressure gauge（4）It is arranged on safety valve（5）And gas-liquid separation chamber（17）Between；The housing（14）In be provided with water bath（15）, water bath（15）It is arranged on gas-liquid separation chamber（17）Lower section, water bath（15）It is connected with electric heater（11）, and electric heater（11）It is arranged on housing（14）Outside is simultaneously fixed on housing（14）Outer wall on；The heat-exchange tube（18）Thermocouple is provided with the disk-like structure of formation（3）, thermocouple（3）Bottom be inserted in housing（14）In；The housing（14）Outside is provided with electric control box（7）And terminal box（8）, and electric control box（7）And terminal box（8）It is connected with each other, electric control box（7）With and electric heater（11）Connection, thermocouple（3）And pressure regulator（6）And electric control box（7）Connection；The housing（14）It is internally provided with liquid level sensor（19）And temperature sensor（20）, liquid level sensor（19）And temperature sensor（20）And electric control box（7）Connection；The housing（14）It is internally provided with blowdown plate（16）, blowdown plate（16）By housing（14）It is divided into two sealed chambers, blowdown plate（16）It is arranged on gas-liquid separation chamber（17）, heat-exchange tube（18）And water bath（15）Lower section, blowdown plate（16）Top surface towards housing（14）Bottom surface is recessed, blowdown plate（16）Center be provided with drainpipe（13）, drainpipe（13）One end passes through blowdown plate（16）With housing（14）Inside connection, the other end passes through housing（14）It is arranged on housing（14）It is outside;Liquid enters housing（14）In heat-exchange tube（18）Before, by liquid filtration device（1）Filtered, worked as liquid inlet electromagnetic valve（2）After experiencing liquid entrance, signal is just transported to terminal box（8）In, so that electric control box（7）Control anti-explosion electric heater（11）And thermocouple（3）Proceed by heating, heat-exchange tube（18）Heat is swapped so that liquid gasification；Liquid after gasification is in gas-liquid separation chamber（17）Separated, gas passes through escaping pipe（21）The place of needs is transported to, during gas transmission out, by safety valve（5）And pressure regulator（6）For escaping pipe（21）The atmospheric pressure value of outlet is adjusted, after after work for a period of time, gas-liquid separation chamber（17）In need cleaning when, by blow-off pipe（10）Carry out sewage treatment, and housing（14）In water then pass through drainpipe（13）Discharge, due to the accumulation of impurity, drainpipe（13）Sewage cannot be discharged, sewage drainpipe can be imported into cleaning（13）In so that housing（14）Inside is cleaned, overflow pipe（12）It is to prevent housing（14）Middle water level is too high to cause internal pressure excessive and design discharge water, limits its peak level, liquid level sensor（19）And temperature sensor（20）It is that liquid level and temperature are monitored, the numerical value that will be detected is timely fed back to electric control box（7）In, it is adjusted according to numerical value set in advance, it is ensured that housing（14）In liquid level and temperature in rational scope.
2. the high steam round-robin method that a kind of water power according to claim 1 exchanges heat, it is characterised in that：The housing（14）In be provided with overflow pipe（12）, overflow pipe（12）With housing（14）Inside connection, and overflow pipe（12）With housing（14）One end of inside connection is near housing（14）Top.
3. the high steam round-robin method that a kind of water power according to claim 1 exchanges heat, it is characterised in that：The housing（14）In be provided with water level controller（9）, heat-exchange tube（18）It is arranged on housing（14）Liquid inlet electromagnetic valve is provided with outside one end（2）With liquid filtration device（1）, liquid inlet electromagnetic valve（2）, thermocouple（3）And water level controller（9）And terminal box（8）Connection.
4. the high steam round-robin method that a kind of water power according to claim 1 exchanges heat, it is characterised in that：The gas-liquid separation chamber（17）In be provided with blow-off pipe（10）, blow-off pipe（10）One end be arranged on housing（14）It is outside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510793788.0A CN106705023A (en) | 2015-11-17 | 2015-11-17 | Water-electricity heat exchange high-pressure steam circulating method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510793788.0A CN106705023A (en) | 2015-11-17 | 2015-11-17 | Water-electricity heat exchange high-pressure steam circulating method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106705023A true CN106705023A (en) | 2017-05-24 |
Family
ID=58932278
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510793788.0A Pending CN106705023A (en) | 2015-11-17 | 2015-11-17 | Water-electricity heat exchange high-pressure steam circulating method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106705023A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114198639A (en) * | 2021-11-26 | 2022-03-18 | 南通恒信达冷冻设备有限公司 | Automatic invariable system of ultra-low temperature liquid basin pressure |
-
2015
- 2015-11-17 CN CN201510793788.0A patent/CN106705023A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114198639A (en) * | 2021-11-26 | 2022-03-18 | 南通恒信达冷冻设备有限公司 | Automatic invariable system of ultra-low temperature liquid basin pressure |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207214413U (en) | A kind of energy-saving electromagnetic boiler | |
| CN106705023A (en) | Water-electricity heat exchange high-pressure steam circulating method | |
| CN205102417U (en) | Electric heated gas ization mechanism of integration control | |
| CN205102095U (en) | System based on carry on heated gas ization to liquid | |
| CN101592400B (en) | High-temperature air stainless steel tube electric heater | |
| CN205102415U (en) | Electric heated gas ization structure that can raise efficiency | |
| CN106705024A (en) | High-pressure steam circulation system for hydroelectric heat transfer | |
| CN202214221U (en) | Phosphorus oxychloride purification device | |
| CN106693409A (en) | Liquid evaporation control method employing water and electricity heat exchange | |
| CN106693410A (en) | Liquid evaporation control system based on hydroelectric heat exchange | |
| CN106705011A (en) | Water-electricity heat exchanging heat cycling system | |
| CN106705012A (en) | Water-electricity heat exchange heat circulation method | |
| CN105258096A (en) | Liquid heating and gasifying system | |
| CN105423262A (en) | Water-electricity heat exchange type high-pressure steam circulating system | |
| CN105413202A (en) | Liquid evaporation control system through hydroelectric heat exchange | |
| CN108291778A (en) | The plasma boiler of tail gas closed loop ionization combustion | |
| CN103172067B (en) | Cold wall fluidized bed and application thereof | |
| CN105258348A (en) | Electrical heating vaporization mechanism | |
| CN105333412A (en) | Heat cycle system with hydroelectric heat exchange function | |
| CN105258349A (en) | Efficient electrical heating vaporization structure | |
| CN212347758U (en) | Durene separation reation kettle | |
| CN205980755U (en) | Drying device of solar wafer fritting furnace | |
| CN109423631B (en) | Vapor deposition uniform heating device and vapor deposition furnace | |
| CN207294178U (en) | A kind of recuperation of heat sulfur burner | |
| CN207936091U (en) | The energy saving runner of infusibility garbage disposal special type incinerator fusant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170524 |
|
| WD01 | Invention patent application deemed withdrawn after publication |