CN102628587B - Phase change heating heat machine and heating method by using phase change heating heat machine - Google Patents
Phase change heating heat machine and heating method by using phase change heating heat machine Download PDFInfo
- Publication number
- CN102628587B CN102628587B CN201210118987.8A CN201210118987A CN102628587B CN 102628587 B CN102628587 B CN 102628587B CN 201210118987 A CN201210118987 A CN 201210118987A CN 102628587 B CN102628587 B CN 102628587B
- Authority
- CN
- China
- Prior art keywords
- water
- phase transformation
- heat
- negative pressure
- heat exchanger
- 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
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The invention discloses a phase change heating heat machine. A water return opening of a heat supply pressure boosting circulating pump (4) is connected with a water inlet (9) arranged at the top of a phase change heater (2) through a first pressure pipe (7) of a first water return branch after flow division, an air outlet (8) arranged at the bottom of the phase change heater (2) is connected with an air inlet (10) of a negative pressure heat exchanger (3), the other branch of a second water return branch is connected with a water inlet of the negative pressure heat exchanger (3), a pressure regulating valve (12) is positioned between the water inlet of the negative pressure heat exchanger (3) and the heat supply pressure boosting circulating pump (4), and a mixed outlet of the negative pressure heat exchanger (3) is sequentially connected with a hot water inlet of a heating load (5) and a water replenishing box (1). The heating method comprises the following steps that: water of the water replenishing box (1) completes the water phase change process by passing the phase change heater, water vapor is conveyed into the negative pressure heat exchanger (3) through an air outlet arranged at the bottom of the phase change heater (2), the pressure regulating valve (12) is opened, the other path of cold water enters the negative pressure heat exchanger (3) after passing through the pressure regulating valve (12) and a second pressure pipe (11), and the water vapor is subjected to heat exchange with cold water in the negative pressure heat exchanger (3) and then flows back into the water replenishing box (1) to be cyclically utilized.
Description
Technical field
A kind of method that the present invention relates to phase transformation heating heat engine and utilize phase transformation heating heat engine to heat.
Background technology
Utilize boiler heat production existing for a long time, for improving function, efficiency, the pollutant emission of boiler, safe operation, all drops into a large amount of manpower and materials in scientific research, production, installation, operation department.Also proceed now this respect work.Comprise the research of the aspects such as boiler material, version, control method, environmental pollution.Safe operation of the boiler, supervision all have strict regulation.But boiler all the time safety, energy resource consumption, Study on environmental pollution is focused on problem.Under the hard and fast rule of national Lee's energy-saving and emission-reduction, some miniature boilers are removed, be incorporated to large-scale centralized heating system, in succession develop large-scale heat pump central heating system simultaneously, earth source heat pump, sea-water heat-pump, sewage water heat pump is waited until system, these measures are to solve the heating problem that people are concerned about, but more there are problems: 1, current heating equipment has unified supplying between the stopping time, if but change and just can not get heating for rear weather for front stopping, and terminal temperature difference temperature there will be phenomenon not up to standard, use inconvenience thereby cause, can not adapt to the demand of heating, 2, working clan's time and the contradiction of actual heating duration, due to discontinuity heating, in family, the old and the children can not get heating, household metering problem is actual unreasonable by hot expense, 3, this equipment there will be outer net heat waste and the impact on environment, and not only result of use is poor, and investment is large, and cost is high, big for environment pollution, construction costs is large in addition, and the security in outer net when maintenance is poor, and the generation that works the mischief to people is leaked in frequently maintenance, if 4 to the high-end house away from central heating region and occupancy rate is low, a large amount of vacant or uninhabited groups building, by there will be cannot heat supply situation, 5, start-up time longer, consumed mass energy, 6, enabling of great lot of water resources, high-quality water resource waste.
Summary of the invention
A kind of method that the invention provides phase transformation heating heat engine and utilize phase transformation heating heat engine to heat, it is good energy-conserving effect not only, and pollution-free, safe, meets national energy-saving and reduces discharging requirement.
The present invention has adopted following technical scheme: a kind of phase transformation heating heat engine, it is characterized in that it comprises into water equipment, water supply tank, phase transformation heater, negative pressure heat exchanger, heat supply supercharging circulating pump, for heat load and power supply and automation control module, the control end of phase transformation heater, the control end of the control end of heat supply supercharging circulating pump and confession heat load is all connected with power supply and automation control module, water inlet equipment is connected with water supply tank, the cold water delivery port of water supply tank is connected with the water inlet of heat supply supercharging circulating pump, the exit of heat supply supercharging circulating pump water return outlet splits into backwater branch road I and backwater branch road II, backwater branch road I comprises force pipe I, heat supply supercharging circulating pump water return outlet is connected with the water inlet at phase transformation heater top by the force pipe I of backwater branch road I, the gas outlet that phase transformation heater base is provided with is connected with the air inlet of negative pressure heat exchanger, backwater branch road II comprises force pipe II and pressure-regulating valve, backwater branch road II is connected with the water inlet of negative pressure heat exchanger, pressure-regulating valve is between heat supply supercharging circulating pump and the water inlet of negative pressure heat exchanger, the mixed export of negative pressure heat exchanger is connected successively with for the hot water inlet of heat load and water supply tank, the cold water of water supply tank splits into two-way after the extraction of heat supply supercharging circulating pump, one road cold water is transported in phase transformation heater by force pipe I, in phase transformation heater through atomization and heating after form water vapour, water vapour is transported in negative pressure heat exchanger by the gas outlet of phase transformation heater base, another road cold water enters in negative pressure heat exchanger after by pressure-regulating valve and force pipe II, water vapour and cold water carry out by the mixed export of negative pressure heat exchanger, the hot water after heat exchange being back in water supply tank successively after supplying heat load after heat exchange.
Described phase transformation heater is set to internal heat type phase transformation device, internal heat type phase transformation device is provided with housing, bottom at housing inner chamber is provided with ring flange, on ring flange, be inserted with some dry combustion method stainless steel electrothermal tubes, be enclosed with alumina silicate heat-insulation layer in whole housing outer surface, the water inlet of case top is provided with atomizer, and gas outlet is positioned at the other end of housing.
Described housing is carbon steel pipes or stainless-steel pipe.Described power supply and automation control module are connected with the control end of phase transformation heater with temperature control line I by power line I.Described power supply and automation control module are connected with the control end of heat supply supercharging circulating pump by power line II.Described power supply and automation control module are connected with the control end for heat load by two temperature control line III.Described power supply and automation control module are set to PLC controller.
The invention discloses a kind of method of utilizing the heating of phase transformation heating heat engine, it comprises the following steps:
Step 1, water source in water supply tank splits into two branch roads successively after the extraction of heat supply supercharging circulating pump, one road cold water is transported in phase transformation heater by force pipe I, cold water enters in phase transformation heater and carries out forming atomized steam after atomization through the atomizer of phase transformation heater, atomized steam produces very strong interior energy, then the water after atomization is sprayed in phase transformation heater and to be heated to 100-400 DEG C through dry combustion method stainless steel electrothermal tube, hydrone particle expands under the state of heating, hydrone particle after expansion becomes water vapour in moment, complete the phase transition process of water, the Energy Efficiency Ratio that atomized steam produces heat in the process that becomes water vapour reaches 1:1.5-3, water vapour is transported in negative pressure heat exchanger by the gas outlet of phase transformation heater base, open pressure-regulating valve, another road cold water enters in negative pressure heat exchanger after by pressure-regulating valve and force pipe II,
Step 2, water vapour and cold water are back to the hot water after heat exchange in water supply tank and recycle successively at the mixed export by negative pressure heat exchanger after negative pressure heat exchanger carries out heat exchange after supplying heat load, have completed like this process of heating, utilization and the circulation of hot water.
The present invention has following beneficial effect: the present invention is provided with phase transformation heater, cold water can be entered into like this to phase transformation heater and after atomizer atomization, form small water smoke, then under the condition of high temperature in phase transformation heater, heat absorption moment becomes steam and discharges, in phase transformation device, complete the phase transition process of water, 1 DEG C of needs 1kcal of the every rising of 1kg water like this, and the water of 100 DEG C only needs 538kcal heat energy while becoming the steam of 100 DEG C, by phase change technique have interior can water and at the systemic heat of phase transformation device, efficiency several times are increased, greatly saved the energy.Water vapor enters load operation system through producing negative pressure carbonated drink interchanger.According to operational system requirement, can normal pressure, have the closed circuit open circuit of pressure (low pressure) all can.Configuration can provide hot water simultaneously as required, and system running, does not need peripheral energy supplement, and according to system requirements, it can be not only normal pressure, have pressure (low pressure) to meet systemic circulation, greatly reduces investment and outer net heat loss; The present invention is provided with power supply and automation control module, between power supply and automation control module, be connected with the control end of phase transformation heater with temperature control line I by power line I, between power supply and automation control module, be connected with the control end of heat supply supercharging circulating pump by power line II, between power supply and automation control module, be connected with the control end for heat load with temperature control line III by power line III, it can adopt automatic control technology, follow the tracks of design temperature, system temperature is adjustable, start shooting at any time, shut down, cold machine start heating time <3min; Water quality does not need softening processing, and bitter alkali water, seawater all can connect use; Standard module assembly, charge-coupled according to load module; Easy to maintenance, except consumable accessory, complete machine service life is more than 20 years.
The parameter of the each module of the present invention is:
。
Brief description of the drawings
Fig. 1 is structural representation of the present invention.
Fig. 2 is control block diagram of the present invention.
Fig. 3 is the structural representation of phase transformation heater of the present invention.
Detailed description of the invention
At Fig. 1, in Fig. 2 and Fig. 3, the invention provides a kind of phase transformation heating heat engine, it comprises into water equipment, water supply tank 1, phase transformation heater 2, negative pressure heat exchanger 3, heat supply supercharging circulating pump 4, for heat load 5 and power supply and automation control module 6, the control end of phase transformation heater 2, the control end of the control end of heat supply supercharging circulating pump 4 and confession heat load 5 is all connected with power supply and automation control module 6, power supply and automation control module 6 are set to PLC controller, power supply and automation control module 6 are connected with the control end of phase transformation heater 2 with temperature control line I 17 by power line I 16, power supply and automation control module 6 are connected with the control end of heat supply supercharging circulating pump 4 by power line II 18, power supply and automation control module 6 are connected with the control end for heat load 5 by two temperature control line III 19, water inlet equipment is connected with water supply tank 1, the cold water delivery port of water supply tank 1 is connected with the water inlet of heat supply supercharging circulating pump 4, the exit of heat supply supercharging circulating pump 4 water return outlets splits into backwater branch road I and backwater branch road II, backwater branch road I comprises force pipe I 7, heat supply supercharging circulating pump 4 water return outlets are connected with the water inlet 9 at phase transformation heater 2 tops by the force pipe I 7 of backwater branch road I, the gas outlet 8 that phase transformation heater 2 bottoms are provided with is connected with the air inlet 10 of negative pressure heat exchanger 3, backwater branch road II comprises force pipe II 11 and pressure-regulating valve 12, backwater branch road II is connected with the water inlet of negative pressure heat exchanger 3, pressure-regulating valve 12 is between heat supply supercharging circulating pump 4 and the water inlet of negative pressure heat exchanger 3, the mixed export of negative pressure heat exchanger 3 is connected successively with for the hot water inlet of heat load 5 and water supply tank 1, the cold water of water supply tank 1 splits into two-way after the extraction of heat supply supercharging circulating pump 4, one road cold water is transported in phase transformation heater 2 by force pipe I 7, phase transformation heater 2 interior through atomization and heating after form water vapour, water vapour is transported in negative pressure heat exchanger 3 by the gas outlet of phase transformation heater 2 bottoms, another road cold water enters in negative pressure heat exchanger 3 after by pressure-regulating valve 12 and force pipe II 11, water vapour and cold water carry out by the mixed export of negative pressure heat exchanger 3, the hot water after heat exchange being back in water supply tank 1 successively after supplying heat load 5 after heat exchange, phase transformation heater 2 is set to internal heat type phase transformation device, internal heat type phase transformation device is provided with housing 13, housing 13 is carbon steel pipes or stainless-steel pipe, bottom at housing 13 inner chambers is provided with ring flange 20, on ring flange 20, be evenly inserted with 12 dry combustion method stainless steel electrothermal tubes 14, be enclosed with alumina silicate heat-insulation layer at whole housing 13 outer surfaces, water inlet 9 places at housing 13 tops are provided with atomizer 15, gas outlet 8 is positioned at the other end of housing 13.
In Fig. 2, the present invention also provides a kind of method of utilizing the heating of phase transformation heating heat engine, it comprises the following steps: step 1, water source in water supply tank 1 splits into two branch roads successively after the extraction of heat supply supercharging circulating pump 4, one road cold water is transported in phase transformation heater 2 by force pipe I 7, cold water enters into the interior atomizer 15 through phase transformation heater 2 of phase transformation heater 2 to carry out forming atomized steam after atomization, atomized steam produces very strong interior energy, then the water after atomization is sprayed into phase transformation heater 2 is interior is heated to 100-400 DEG C through dry combustion method stainless steel electrothermal tube 14, hydrone particle expands under the state of heating, hydrone particle after expansion becomes water vapour in moment, complete the phase transition process of water, the Energy Efficiency Ratio that atomized steam produces heat in the process that becomes water vapour reaches 1:1.5-3, water vapour is transported in negative pressure heat exchanger 3 by the gas outlet of phase transformation heater 2 bottoms, open pressure-regulating valve 12, another road cold water enters in negative pressure heat exchanger 3 after by pressure-regulating valve 12 and force pipe II 11, step 2, water vapour and cold water are back to the hot water after heat exchange in water supply tank 1 and recycle successively at the mixed export by negative pressure heat exchanger 3 after negative pressure heat exchanger 3 carries out heat exchange after supplying heat load 5, have completed like this process of heating, utilization and the circulation of hot water.
Claims (7)
1. a phase transformation heating heat engine, it is characterized in that it comprises into water equipment, water supply tank (1), phase transformation heater (2), negative pressure heat exchanger (3), heat supply supercharging circulating pump (4), for heat load (5) and power supply and automation control module (6), the control end of phase transformation heater (2), the control end of the control end of heat supply supercharging circulating pump (4) and confession heat load (5) is all connected with power supply and automation control module (6), water inlet equipment is connected with water supply tank (1), the cold water delivery port of water supply tank (1) is connected with the water inlet of heat supply supercharging circulating pump (4), the exit of heat supply supercharging circulating pump (4) water return outlet splits into backwater branch road I and backwater branch road II, backwater branch road I comprises force pipe I (7), heat supply supercharging circulating pump (4) water return outlet is connected with the water inlet (9) at phase transformation heater (2) top by the force pipe I (7) of backwater branch road I, the gas outlet (8) that phase transformation heater (2) bottom is provided with is connected with the air inlet (10) of negative pressure heat exchanger (3), backwater branch road II comprises force pipe II (11) and pressure-regulating valve (12), backwater branch road II is connected with the water inlet of negative pressure heat exchanger (3), pressure-regulating valve (12) is positioned between heat supply supercharging circulating pump (4) and the water inlet of negative pressure heat exchanger (3), the mixed export of negative pressure heat exchanger (3) is connected successively with for the hot water inlet of heat load (5) and water supply tank (1), the cold water of water supply tank (1) splits into two-way after the extraction of heat supply supercharging circulating pump (4), one road cold water is transported in phase transformation heater (2) by force pipe I (7), in phase transformation heater (2) through atomization and heating after form water vapour, water vapour is transported in negative pressure heat exchanger (3) by the gas outlet of phase transformation heater (2) bottom, another road cold water enters in negative pressure heat exchanger (3) after by pressure-regulating valve (12) and force pipe II (11), water vapour and cold water carry out by the mixed export of negative pressure heat exchanger (3), the hot water after heat exchange being back in water supply tank (1) successively after supplying heat load (5) after heat exchange, described phase transformation heater (2) is set to internal heat type phase transformation device, internal heat type phase transformation device is provided with housing (13), bottom at housing (13) inner chamber is provided with ring flange (20), on ring flange (20), be inserted with some dry combustion method stainless steel electrothermal tubes (14), be enclosed with alumina silicate heat-insulation layer at whole housing (13) outer surface, the water inlet (9) at housing (13) top locates to be provided with atomizer (15), gas outlet (8) is positioned at the other end of housing (13).
2. phase transformation heating heat engine according to claim 1, is characterized in that described housing (13) is carbon steel pipes or stainless-steel pipe.
3. phase transformation heating heat engine according to claim 1, is characterized in that described power supply and automation control module (6) are connected with the control end of phase transformation heater (2) with temperature control line I (17) by power line I (16).
4. phase transformation heating heat engine according to claim 1, is characterized in that described power supply and automation control module (6) are connected with the control end of heat supply supercharging circulating pump (4) by power line II (18).
5. phase transformation heating heat engine according to claim 1, is characterized in that described power supply and automation control module (6) are connected with the control end that supplies heat load (5) by two temperature control line III (19).
6. according to the phase transformation heating heat engine described in claim 1,3,4 or 5, it is characterized in that described power supply and automation control module (6) are set to PLC controller.
7. a method of utilizing the heating of phase transformation heating heat engine, it comprises the following steps:
Step 1, water source in water supply tank (1) splits into two branch roads successively after the extraction of heat supply supercharging circulating pump (4), one road cold water is transported in phase transformation heater (2) by force pipe I (7), cold water enters in phase transformation heater (2) and carries out forming atomized steam after atomization through the atomizer (15) of phase transformation heater (2), atomized steam produces very strong interior energy, then the water after atomization is sprayed in phase transformation heater (2) and to be heated to 100-400 DEG C through dry combustion method stainless steel electrothermal tube (14), hydrone particle expands under the state of heating, hydrone particle after expansion becomes water vapour in moment, complete the phase transition process of water, the Energy Efficiency Ratio that atomized steam produces heat in the process that becomes water vapour reaches 1:1.5-3, water vapour is transported in negative pressure heat exchanger (3) by the gas outlet of phase transformation heater (2) bottom, open pressure-regulating valve (12), another road cold water enters in negative pressure heat exchanger (3) after by pressure-regulating valve (12) and force pipe II (11),
Step 2, water vapour and cold water are back to the hot water after heat exchange in water supply tank (1) and recycle successively at the mixed export by negative pressure heat exchanger (3) after negative pressure heat exchanger (3) carries out heat exchange after for heat load (5), have completed like this process of heating, utilization and the circulation of hot water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210118987.8A CN102628587B (en) | 2012-04-23 | 2012-04-23 | Phase change heating heat machine and heating method by using phase change heating heat machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210118987.8A CN102628587B (en) | 2012-04-23 | 2012-04-23 | Phase change heating heat machine and heating method by using phase change heating heat machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102628587A CN102628587A (en) | 2012-08-08 |
| CN102628587B true CN102628587B (en) | 2014-10-08 |
Family
ID=46586905
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210118987.8A Expired - Fee Related CN102628587B (en) | 2012-04-23 | 2012-04-23 | Phase change heating heat machine and heating method by using phase change heating heat machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102628587B (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH656202A5 (en) * | 1982-03-15 | 1986-06-13 | Schoenmann Wilfred Ernst | Steam boiler with electric resistance heating |
| JP2008025981A (en) * | 2006-07-20 | 2008-02-07 | Ogura Tekko Kk | Through flow boiler for steam washer |
| CN201028493Y (en) * | 2007-04-18 | 2008-02-27 | 王云龙 | Multifunctional phase-change boiler |
| CN101358729A (en) * | 2007-07-26 | 2009-02-04 | 曹国铉 | Apparatus for generating steam |
| CN101871043A (en) * | 2010-06-25 | 2010-10-27 | 东莞市康汇聚线材科技有限公司 | Steam generator of annealing furnace and control method thereof |
| CN203162911U (en) * | 2012-04-23 | 2013-08-28 | 王兔林 | Phase change heating heat machine |
-
2012
- 2012-04-23 CN CN201210118987.8A patent/CN102628587B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH656202A5 (en) * | 1982-03-15 | 1986-06-13 | Schoenmann Wilfred Ernst | Steam boiler with electric resistance heating |
| JP2008025981A (en) * | 2006-07-20 | 2008-02-07 | Ogura Tekko Kk | Through flow boiler for steam washer |
| CN201028493Y (en) * | 2007-04-18 | 2008-02-27 | 王云龙 | Multifunctional phase-change boiler |
| CN101358729A (en) * | 2007-07-26 | 2009-02-04 | 曹国铉 | Apparatus for generating steam |
| CN101871043A (en) * | 2010-06-25 | 2010-10-27 | 东莞市康汇聚线材科技有限公司 | Steam generator of annealing furnace and control method thereof |
| CN203162911U (en) * | 2012-04-23 | 2013-08-28 | 王兔林 | Phase change heating heat machine |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102628587A (en) | 2012-08-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202051511U (en) | Steaming equipment | |
| CN103557509A (en) | Intelligent steam generator | |
| CN207648835U (en) | A kind of boiler exhaust gas waste heat recovery heat supply three towers unification heat transfer spray tower | |
| CN103657329A (en) | Yellow phosphorus exhaust gas centralized control, recycling and purifying device | |
| CN203162911U (en) | Phase change heating heat machine | |
| CN103644032A (en) | System for heating natural gas through gradient utilization of water supplied at medium pressure from waste heat boiler of gas turbine power plant | |
| CN205291235U (en) | Component steam maintenance system | |
| CN102628587B (en) | Phase change heating heat machine and heating method by using phase change heating heat machine | |
| CN206669688U (en) | A kind of multichannel exhaust-heat boiler system equipment | |
| CN201901806U (en) | Closed type waste heat recovery system of corrugated paperboard production line | |
| CN202647703U (en) | Efficient low-energy steam generation device | |
| CN205261518U (en) | Steaming system | |
| CN102679311A (en) | Steam generation device with high efficiency and low energy consumption | |
| CN210570082U (en) | Water-saving system of cooling tower of thermal power plant | |
| CN209128296U (en) | Sludge dry system | |
| CN203798205U (en) | Industrial waste gas waste heat-recycling heat exchanging device | |
| CN202938281U (en) | Solar energy-electric heat combined steam generation and residual heat recycling device | |
| CN206386911U (en) | A kind of chemical water heating system | |
| CN105444243A (en) | Waste heat recovery heat supply and water charging system and water charging method | |
| CN103868377B (en) | Industrial waste gas waste heat recovery heat-exchanger rig | |
| CN202993164U (en) | Boiler blowdown heat utilization device | |
| CN109368973A (en) | Sludge dry system | |
| CN203162910U (en) | Phase change heat engine | |
| CN203686984U (en) | Solar gas boiler system | |
| CN202203917U (en) | Tail steam recycling system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180723 Address after: 461100 Xuchang, Henan (Xuchang County, Shang Ji industrial agglomeration area Binhe Road) Patentee after: Xuchang Han Sheng Energy Technology Co., Ltd. Address before: No. 19, Nantong Road, Hailing District, Taizhou, Jiangsu Patentee before: Wang Tulin |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141008 Termination date: 20210423 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |