CN102721033A - Non-metallic energy oil steam generation method and generation device of no-pressure container - Google Patents
Non-metallic energy oil steam generation method and generation device of no-pressure container Download PDFInfo
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- CN102721033A CN102721033A CN2012101389588A CN201210138958A CN102721033A CN 102721033 A CN102721033 A CN 102721033A CN 2012101389588 A CN2012101389588 A CN 2012101389588A CN 201210138958 A CN201210138958 A CN 201210138958A CN 102721033 A CN102721033 A CN 102721033A
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Abstract
The invention discloses a non-metallic energy oil steam generation method and a generation device of a no-pressure container. The method comprises the following steps: a high carbon molecular non-metallic energy oil is heated and gasified, and the gasified high carbon molecular non-metallic energy oil is compressed by using a compressor so as to be transformed into a high temperature gaseous form of high carbon molecular non-metallic energy oil; the transformed high carbon molecular non-metallic energy oil enters a heat exchange pipe to exchange energy with liquid water so as to evaporate the liquid water; and the gaseous high carbon molecular non-metallic energy oil enters a heat exchanger and is transformed into a liquid form of high carbon molecular non-metallic energy oil, and the liquid form of high carbon molecular non-metallic energy oil enters an oil tank again for circulation operations. The invention further discloses the non-metallic energy oil steam generation device of the no-pressure container, wherein the device is designed according to the above-mentioned method. The method of the invention is simple, and has advantages of simple device operation implementation means, rapid steam generation, environmental protection, low manufacturing cost, small size and good safety performance.
Description
Technical field
The present invention relates to the steam generation technical field, refer to a kind of no pressure vessel nonmetal energy oil vapour method for generation and generation equipment particularly.
Background technology
Existing steam raising plant has gas fired-boiler, oil burning boiler, coal-burning boiler, coal water slurry boiler, electric boiler; This apparatus structure is complicated, all necessary store water heating evaporation, and energy consumption is high, efficient is low; And all belong to pressure vessel, its drum and miscellaneous part all need bear very big internal pressure.Pressure vessel is owing to reasons such as sealing, pressure-bearing and media, is easy to generate blast, burning is on fire and jeopardize the safety of personnel, equipment and property and the accident of contaminated environment, and is dangerous; Dangerous big, environmental pollution is big, and owing to determined by the character of water; Can't improve vapor (steam) temperature, investment is big, and heat time heating time is long; Energy-output ratio is big, and the consumption of water is big, and efficient is low.
Summary of the invention
The object of the invention is exactly the deficiency that will solve the above-mentioned background technology, and a kind of no pressure vessel nonmetal energy oil vapour method for generation and generation equipment are provided.
Technical scheme of the present invention is:
The nonmetal energy oil vapour of a kind of no pressure vessel method for generation comprises following steps:
1), high carbon molecule nonmetal can gauging in oil cylinder behind heating and gasifying, be converted into gaseous form, after compressor sucked compression, temperature further raise, forming that the gaseous state high carbon molecule of compression is nonmetal can gauging;
2), nonmetal can gauging entering in the gas-liquid heat exchanging pipe of gaseous state high carbon molecule of compression, in the gas-liquid heat exchanging pipe,, and then make aqueous water be converted into steam condition with the aqueous water positive energy exchange;
3), with the aqueous water energy exchange after the gaseous state high carbon molecule nonmetal can gauging, get in the heat exchanger, make that the high carbon molecule of gaseous form is nonmetal to be converted into liquid form by gauging, flow in the oil cylinder to carry out next circulation.
In such scheme:
At compressor when nonmetal energy oil pressure contracts to high carbon molecule; Through the nonmetal ability of the liquid high carbon molecule of gear pump after liquid liquid heat exchanging pipe is carried heating gauging; In liquid liquid heat exchanging pipe,, and then make aqueous water be converted into steam condition with the aqueous water positive energy exchange.
The same rotating shaft of described gear pump and compressor.
In said step (3), the high carbon molecule of liquid form is nonmetal to be back in the oil gas case of establishing in the oil cylinder by gauging.
Further; After the heating of the nonmetal ability of the high carbon molecule of the liquid state in said oil gas case gauging; Through the nonmetal ability of the liquid high carbon molecule of gear pump after liquid liquid heat exchanging pipe is carried heating gauging; In liquid liquid heat exchanging pipe,, and then make aqueous water be converted into steam condition with the aqueous water positive energy exchange.
The nonmetal energy oil vapour of a kind of no pressure vessel generation equipment; Comprise apparatus casing, on described apparatus casing, be provided with base, on base, be provided with oil cylinder; Said oil cylinder is provided with the air communication mouth; Be provided with the nonmetal ability of liquid high carbon molecule gauging in the oil cylinder, have void layer between the end face on nonmetal energy oil level of high carbon molecule and the oil cylinder, also be provided with the oil gas case of heating element heater, liquid liquid heat exchanging pipe, gas-liquid heat exchanging pipe and open upper end at oil cylinder; Be provided with high-pressure hydraulic pump, continuous gear pump and the compressor in axle center in the apparatus casing; Described heating element heater is deep in the nonmetal ability of the high carbon molecule gauging, and an end of gear pump is connected with the oil gas case through oil inlet pipe, and the other end of gear pump is connected through the oil reservoir pipeline in flowline and the liquid liquid heat exchanging pipe; Compressor one end is connected through the void layer of air inlet pipe and oil cylinder; The other end of compressor is connected through the oil reservoir pipeline of escape pipe and gas-liquid heat exchanging pipe, and high-pressure hydraulic pump is through the water layer pipeline connection of aqueduct and liquid liquid heat exchanging pipe, gas-liquid heat exchanging pipe; The oil reservoir pipeline upper end of gas-liquid heat exchanging pipe is connected with heat exchanger through high-pressure air pipe, and the outlet of heat exchanger is communicated with the opening part of oil gas case, and the oil reservoir pipeline of liquid liquid heat exchanging pipe is provided with oil exit pipe; The water layer pipeline of liquid liquid heat exchanging pipe, gas-liquid heat exchanging pipe is provided with steam (vapor) outlet.
Further; Described liquid liquid heat exchanging pipe and gas-liquid heat exchanging pipe are the spiral double-skin duct; The oil reservoir pipeline of liquid liquid heat exchanging pipe and gas-liquid heat exchanging pipe is the inner layer pipe of spiral double-skin duct, and the water layer pipeline of liquid liquid heat exchanging pipe and gas-liquid heat exchanging pipe is the outer layer pipe of spiral double-skin duct.
Preferably, the water layer pipeline of the water layer pipeline of described liquid liquid heat exchanging pipe and gas-liquid heat exchanging pipe is connected.
High carbon molecule of the present invention is nonmetal gauging to be existing product.
Method for generation of the present invention is through can gauging passing through compressor compresses behind the heating and gasifying with high carbon molecule is nonmetal; Make it be converted into the high-temperature gas form; High carbon molecule after the conversion is nonmetal can gauging to be got in the gas-liquid heat exchanging pipe and the aqueous water positive energy exchange; And then make aqueous water produce evaporation, and the high carbon molecule of gaseous state is nonmetal can gauging get in the heat exchanger in and be converted into liquid form and get into oil cylinder once more, carry out cycle operation; The present invention also utilizes the compressor axle center to be connected with the gear pump axle center; In the time of the nonmetal ability of the high carbon molecule of compressor compresses gaseous state gauging; Exchange the nonmetal ability of the high carbon molecule gauging that pipeline is carried high temperature through gear pump to liquid liquid, the nonmetal ability of the high carbon molecule in circulating oil cylinder gauging makes integral body exchange temperature even; And replenish relative temperature to compressor head, temperature balance when the nonmetal energy innage of the high carbon molecule temperature and pressure of gasification are contracted.
The nonmetal energy oil vapour of no pressure vessel generation equipment described in the invention, the heat exchanging pipe of employing is the spiral double-skin duct, it serves the high temperature area big, saves the operating cost of energy resource consumption, reduction manufacturing cost and use steam.In addition, its pressure and temperature can reach needed steam pressure and temperature through regulating oily gentle porous water inlet, determined by the character of water.This equipment can make the nonmetal energy fluid of high carbon molecule gas change absorb that the low energy converts high-energy source in the air; Improve heating efficiency and reach cop value 201%; This equipment solves that steam pressure and temperature can not be controlled and regulate for a long time; Boiler can not dry combustion method, and boiler pressure is pressure release and the low problem of the thermal efficiency at short notice.Use the nonmetal energy oil vapour of no pressure vessel generation equipment, energy consumption is little, the thermal efficiency is high, water is few, steam fast, temperature, pressure is controllable.Pressure relief is fool proof fast.Fill up international and domestic blank, this device structure is simple, volume is little, no discharging, environmental protection, can anhydrous dry combustion method and pressure relief fast, fool proof.Be applicable to that all types of units of enterprises and institutions, hotel, hotel, large-scale swimming pipe, laboratory, family use.
Description of drawings
Fig. 1 is method for generation sketch map among the present invention.
The device structure sketch map for taking place in Fig. 2 among the present invention.
Fig. 3 is connected sketch map for compressor among the present invention with gear pump.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment the present invention is done further detailed description, be convenient to be well understood to the present invention, but they do not constitute qualification to the present invention.
As shown in Figure 1, the nonmetal energy oil vapour of a kind of no pressure vessel method for generation: comprise following steps:
1), with high carbon molecule nonmetal can gauging 1 oil cylinder 2 in behind heating element heater 3 heating and gasifyings, be converted into gaseous form, after compressor 4 sucks compression, the temperature of the nonmetal ability of the high carbon molecule of gaseous form gauging is further raise; Simultaneously; Carry through gear pump 5 the nonmetal ability of the high-temperature liquid state high carbon molecule of oil gas case 6 the insides gauging to the oil reservoir pipeline of liquid liquid heat exchanging pipe 22; The nonmetal ability of the high carbon molecule of oil cylinder 2 capable of circulation gauging make whole exchange temperature even, and the axle center of gear pump 5 and compressor 4 links to each other; Replenish relative temperature can for compressor 4 heads, temperature balance when the nonmetal energy innage of the high carbon molecule temperature and pressure of gasification are contracted.
2), the gaseous state high carbon molecule of compression is nonmetal can get into the oil reservoir pipeline in the gas-liquid heat exchanging pipe 22 by gauging; The oil reservoir pipeline of the entering liquid liquid heat exchanging pipe 7 of the nonmetal ability of the high carbon molecule gauging of the liquid form that after gear pump 5 is handled, produces; The water layer pipeline of gas-liquid heat exchanging pipe 22 and liquid liquid heat exchanging pipe 7 is filling the aqueous water of building through high-pressure hydraulic pump 8; Behind the nonmetal ability of the ducted high temperature high carbon molecule of oil reservoir gauging positive energy exchange, from steam (vapor) outlet 9, discharge.
3) after, the nonmetal ability of the high carbon molecule of gaseous state gauging flows out from the oil reservoir pipeline of gas-liquid heat exchanging pipe 22; Get in the heat exchanger 10; In heat exchanger 10, contact with surrounding air; And then the ambient air heat radiation, make the nonmetal ability of the high carbon molecule gauging of gaseous form be converted into liquid form, flow in the oil gas case 6 to carry out next circulation; After the nonmetal ability of the high carbon molecule of liquid form gauging flows out, flow directly into oil cylinder 2, to carry out next circulation from the oil reservoir pipeline of liquid liquid heat exchanging pipe 7.
As shown in Figure 2; The nonmetal energy oil vapour of a kind of no pressure vessel generation equipment comprises apparatus casing 11, on apparatus casing 11, is provided with electric controller 12 and base 13; On base 13, be provided with oil cylinder 2 and support 14; Oil cylinder 2 is provided with air communication mouth 15, in oil cylinder 2, is provided with the nonmetal ability of liquid high carbon molecule gauging, has void layer between the end face on nonmetal energy oil level of high carbon molecule and the oil cylinder 2; In oil cylinder 2, also be provided with the oil gas case 6 of heating element heater 3, liquid liquid heat exchanging pipe 7, gas-liquid heat exchanging pipe 22 and open upper end; On support 14, be provided with high-pressure hydraulic pump 8, the continuous gear pump 5 and compressor 4 in axle center, heating element heater 3 is by electric controller 12 controls, and heating element heater 3 is deep in the nonmetal ability of the high carbon molecule gauging; One end of gear pump 5 is connected with oil gas case 6 through oil inlet pipe 16, and the other end of gear pump 5 is connected through flowline 27 and the oil reservoir pipeline in the liquid liquid heat exchanging pipe 7; Compressor 4 one ends are connected through the air inlet pipe 17 and the void layer of oil cylinder 2; The other end of compressor 4 is connected through the escape pipe 28 and the oil reservoir pipeline of gas-liquid heat exchanging pipe 22, and high-pressure hydraulic pump 8 is connected through the aqueduct 18 and the water layer pipeline of liquid liquid heat exchanging pipe 7, gas-liquid heat exchanging pipe 22; The oil reservoir pipeline upper end of gas-liquid heat exchanging pipe 22 is connected with heat exchanger 10 through high-pressure air pipe 19, and the outlet of heat exchanger 10 is communicated with the opening part of oil gas case 6, and the oil reservoir pipeline of liquid liquid heat exchanging pipe 7 is provided with oil exit pipe 21; The water layer pipeline of liquid liquid heat exchanging pipe 7, gas-liquid heat exchanging pipe 22 is provided with steam (vapor) outlet 9.
As shown in Figure 3, compressor 4 comprises axle center 24, on axle center 24, is fixed with revolving coil 25 and screw pump 26, and an end in axle center 24 is connected with the axle center 27 of gear pump 5, is fixed with gear 23 on the axle center 27.During work; The gear 23 of gear pump 5 will can be gone in the gear pump 5 by dispensing pump from the high carbon molecule that oil guide pipe 16 is carried is nonmetal; The nonmetal ability of high carbon molecule in circulating oil cylinder gauging makes whole exchange temperature even, heats can for simultaneously the head of compressor 4; Replenish relative temperature to it, temperature balance when the nonmetal energy innage of the high carbon molecule temperature and pressure of gasification are contracted.
Liquid liquid heat exchanging pipe 7 in the present embodiment is the spiral double-skin duct with gas-liquid heat exchanging pipe 22; The oil reservoir pipeline of liquid liquid heat exchanging pipe 7 and gas-liquid heat exchanging pipe 22 is the inner layer pipe of spiral double-skin duct; The water layer pipeline of liquid liquid heat exchanging pipe 7 and gas-liquid heat exchanging pipe 22 is the outer layer pipe of spiral double-skin duct; The water layer pipeline of liquid liquid heat exchanging pipe 7 and the water layer pipeline of gas-liquid heat exchanging pipe 22 are connected; The spiral double-skin duct it serve the high temperature area big, saves the operating cost of energy resource consumption, reduction manufacturing cost and use steam.
The inventive method is simple, and equipment operation realization means are simple, and aerogenesis is fast, environmental protection, low cost of manufacture, volume is little, security performance good.
As a kind of distortion of this instance, described oil gas case 6 is arranged on the outside of oil cylinder 2, and promptly oil gas case 6 is a split-type structural with oil cylinder 2.
Claims (8)
1. the nonmetal energy oil vapour of a no pressure vessel method for generation is characterized in that, comprises following steps:
1), high carbon molecule nonmetal can gauging in oil cylinder behind heating and gasifying, be converted into gaseous form, after compressor sucked compression, temperature further raise, forming that the gaseous state high carbon molecule of compression is nonmetal can gauging;
2), nonmetal can gauging entering in the gas-liquid heat exchanging pipe of gaseous state high carbon molecule of compression, in the gas-liquid heat exchanging pipe,, and then make aqueous water be converted into steam condition with the aqueous water positive energy exchange;
3), with the aqueous water energy exchange after the gaseous state high carbon molecule nonmetal can gauging, get in the heat exchanger, make that the high carbon molecule of gaseous form is nonmetal to be converted into liquid form by gauging, flow in the oil cylinder to carry out next circulation.
2. the nonmetal energy oil vapour of no pressure vessel according to claim 1 method for generation; It is characterized in that; At compressor when nonmetal energy oil pressure contracts to high carbon molecule, through the liquid high carbon molecule of gear pump after liquid liquid heat exchanging pipe is carried heating is nonmetal can gauging; At liquid liquid heat exchanging pipe and aqueous water positive energy exchange, and then make aqueous water be converted into steam condition.
3. the nonmetal energy oil vapour of no pressure vessel according to claim 2 method for generation is characterized in that the same rotating shaft of described gear pump and compressor.
4. the nonmetal energy oil vapour of no pressure vessel according to claim 1 method for generation is characterized in that: in the said step (3), the high carbon molecule of liquid form is nonmetal to be back in the oil gas case of establishing in the oil cylinder by gauging.
5. the nonmetal energy oil vapour of no pressure vessel according to claim 4 method for generation; It is characterized in that: after the heating of the nonmetal ability of the high carbon molecule of the liquid state in oil gas case gauging; Through the nonmetal ability of the liquid high carbon molecule of gear pump after liquid liquid heat exchanging pipe is carried heating gauging; At liquid liquid heat exchanging pipe and aqueous water positive energy exchange, and then make aqueous water be converted into steam condition.
6. the nonmetal energy oil vapour of no pressure vessel generation equipment; Comprise apparatus casing (11); On described apparatus casing (11), be provided with base (13); On base (13), be provided with oil cylinder (2); It is characterized in that said oil cylinder (2) is provided with air communication mouth (15), be provided with the nonmetal ability of liquid high carbon molecule gauging in the oil cylinder (2); Nonmetal energy oil level of high carbon molecule and oil cylinder (2) are gone up between the end face has void layer; In oil cylinder (2), also be provided with the oil gas case (6) of heating element heater (3), liquid liquid heat exchanging pipe (7), gas-liquid heat exchanging pipe (22) and open upper end, be provided with high-pressure hydraulic pump (8), the continuous gear pump (5) and compressor (4) in axle center in the apparatus casing (11), described heating element heater (3) is deep in the nonmetal ability of the high carbon molecule gauging; One end of gear pump (5) is connected with oil gas case (6) through oil inlet pipe (16), and the other end of gear pump (5) is connected through flowline (27) and the oil reservoir pipeline in the liquid liquid heat exchanging pipe (7); Compressor (4) one ends are connected through the air inlet pipe (17) and the void layer of oil cylinder (2); The other end of compressor (4) is connected through the escape pipe (28) and the oil reservoir pipeline of gas-liquid heat exchanging pipe (22), and high-pressure hydraulic pump (8) is connected through the aqueduct (18) and the water layer pipeline of liquid liquid heat exchanging pipe (7), gas-liquid heat exchanging pipe (22); The oil reservoir pipeline upper end of gas-liquid heat exchanging pipe (22) is connected with heat exchanger (10) through high-pressure air pipe (19); The outlet of heat exchanger (10) is communicated with the opening part of oil gas case (6), and the oil reservoir pipeline of liquid liquid heat exchanging pipe (7) is provided with oil exit pipe (21); The water layer pipeline of liquid liquid heat exchanging pipe (7), gas-liquid heat exchanging pipe (22) is provided with steam (vapor) outlet (9).
7. according to the nonmetal energy oil vapour of no pressure vessel generation equipment according to claim 6; It is characterized in that; Described liquid liquid heat exchanging pipe (7) and gas-liquid heat exchanging pipe (22) are the spiral double-skin duct; The oil reservoir pipeline of liquid liquid heat exchanging pipe (7) and gas-liquid heat exchanging pipe (22) is the inner layer pipe of spiral double-skin duct, and the water layer pipeline of liquid liquid heat exchanging pipe (7) and gas-liquid heat exchanging pipe (22) is the outer layer pipe of spiral double-skin duct.
8. according to the nonmetal energy oil vapour of no pressure vessel generation equipment according to claim 7, it is characterized in that the water layer pipeline of the water layer pipeline of described liquid liquid heat exchanging pipe (7) and gas-liquid heat exchanging pipe (22) is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210138958.8A CN102721033B (en) | 2012-05-07 | 2012-05-07 | Non-metallic energy oil steam generation method and generation device of no-pressure container |
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| CN201210138958.8A CN102721033B (en) | 2012-05-07 | 2012-05-07 | Non-metallic energy oil steam generation method and generation device of no-pressure container |
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| CN102721033A true CN102721033A (en) | 2012-10-10 |
| CN102721033B CN102721033B (en) | 2014-07-02 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103615917A (en) * | 2013-11-28 | 2014-03-05 | 姜堰市泰怡金属网管有限公司 | Double-layer twisted type heat exchange tube |
| CN105180437A (en) * | 2015-10-10 | 2015-12-23 | 程洪亮 | Liquid-vapor energy device |
| CN105386802A (en) * | 2015-09-28 | 2016-03-09 | 程洪亮 | Modular non-pressure vessel steam generator |
| CN111649311A (en) * | 2020-06-05 | 2020-09-11 | 武汉翊能科技有限公司 | Two-phase non-pressure container water-gas-fired steam engine |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201259205Y (en) * | 2008-08-08 | 2009-06-17 | 程洪亮 | Two-phase heat collection steam engine |
| WO2010003413A2 (en) * | 2008-06-17 | 2010-01-14 | Aalborg Industries A/S | Bypass system for waste heat recovery systems |
| KR20110107969A (en) * | 2010-03-26 | 2011-10-05 | 배승명 | Steam generator |
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2012
- 2012-05-07 CN CN201210138958.8A patent/CN102721033B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010003413A2 (en) * | 2008-06-17 | 2010-01-14 | Aalborg Industries A/S | Bypass system for waste heat recovery systems |
| CN201259205Y (en) * | 2008-08-08 | 2009-06-17 | 程洪亮 | Two-phase heat collection steam engine |
| KR20110107969A (en) * | 2010-03-26 | 2011-10-05 | 배승명 | Steam generator |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103615917A (en) * | 2013-11-28 | 2014-03-05 | 姜堰市泰怡金属网管有限公司 | Double-layer twisted type heat exchange tube |
| CN105386802A (en) * | 2015-09-28 | 2016-03-09 | 程洪亮 | Modular non-pressure vessel steam generator |
| CN105386802B (en) * | 2015-09-28 | 2018-02-27 | 程洪亮 | Modular pressureless force container steam-driven generator |
| CN105180437A (en) * | 2015-10-10 | 2015-12-23 | 程洪亮 | Liquid-vapor energy device |
| CN111649311A (en) * | 2020-06-05 | 2020-09-11 | 武汉翊能科技有限公司 | Two-phase non-pressure container water-gas-fired steam engine |
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| CN102721033B (en) | 2014-07-02 |
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