CN201215351Y - Closed type energy-conserving heating and heat exchanging system - Google Patents
Closed type energy-conserving heating and heat exchanging system Download PDFInfo
- Publication number
- CN201215351Y CN201215351Y CNU2008200803857U CN200820080385U CN201215351Y CN 201215351 Y CN201215351 Y CN 201215351Y CN U2008200803857 U CNU2008200803857 U CN U2008200803857U CN 200820080385 U CN200820080385 U CN 200820080385U CN 201215351 Y CN201215351 Y CN 201215351Y
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- heating
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Abstract
The utility model relates to the heating device technical field, in particular to a closed energy-saving heating and heat-exchanging system. Aiming to overcome the existed problems of high cost, low safety factor and pollution to an oil tank in the prior art, the utility model provides a closed energy-saving and heat-exchanging system which comprises a decompressor, a heat radiator and an oil collecting tank, wherein a heat exchanger is disposed between the decompressor and the heat radiator, and a temperature control valve is arranged between the heat exchanger and the oil collecting tank. Compared with the prior art, the utility model increases safety factor of the heating system, avoids easily hurting personnel and damaging devices, further, can prevent steam from entering the oil collecting tank to cause waste, increases thermal efficiency, and additionally can achieve self-circulation and cost reduction without using external energy.
Description
Technical field
The utility model relates to the heating equipment technical field, is specifically related to a kind of closed energy-saving heating heat-exchange system.
Background technology
By an oil recovery measuring station winter heating is example, at present, adopt high steam direct heating after reducing pressure, be that throttled steam directly enters radiator, after the radiator heat release, enter accumulator tank, have following problem: 1, residual steam enters a jar release, waste heat energy, the cost height: 1 measuring station heating installation is annual to be used 6 months, and 3 monthly average are used steam 20 sides every day when being cold, and used steam 7 sides 3 average every days when weather was not too cold, one side's steam is 78 yuan, measuring station year heating cost be 18.95 ten thousand yuan.2 safety coefficients are low: 180 ℃～230 ℃ of the dry gas temperature that steam boiler produced, pressure 4～8Mpa, and the wall thickness of radiator is little, as once hot spot is arranged, will cause high steam to unload leakage, easily produce casualty accident, the steam after unloading leakage is full of the interior space at short notice, and staff's sight line is unclear, can't withdraw, the personnel that easily cause suffocate.3, after residual steam enters big jar, enter atmosphere through a big jar manhole, steam is taken part crude oil out of oil tank in discharge process, has polluted oil tank, has buried hidden danger again.
Summary of the invention
In order to overcome the problem that the cost height, the safety coefficient that exist in the prior art are low, pollute oil tank, the utility model provides a kind of energy-conservation, cost is low, safety coefficient is high closed energy-saving heating heat-exchange system.
In order to achieve the above object, the technical solution adopted in the utility model is:
A kind of closed energy-saving heating heat-exchange system comprises decompressor, radiator, accumulator tank, and its special character is: be provided with heat exchanger between described decompressor and the radiator, be provided with temperature control valve between heat exchanger and the accumulator tank.
Be provided with the hot and cold water heat exchange box between described temperature control valve and the accumulator tank.
Heat dump in the described heat exchanger is the pawl type.
The heat exchange liquid of filling between described heat exchanger and the heat dump is superconducting fluid.
Compared with prior art, advantage of the present utility model is as follows:
1, the utility model adopts two cyclic designs, and high temperature, high steam do not enter heating system, avoid high temperature, high steam to leak, and the personnel that cause scald or suffocation accident takes place, and have improved the safety coefficient of heating system.
2, heat exchanger safety coefficient height in the utility model, withstand voltage 2.5MPa satisfies the requirement of heating pressure; Heating system adopts negative pressure, low temperature (70 ℃～90 ℃) design, is difficult for causing personnel and equipment damage.
3, the utility model utilizes existing steam decompressor to make low-pressure steam enter heat exchanger, condensed water after the heat exchange enters accumulator tank through autoamtic temperature controlling valve (the control temperature is between 80 ℃～100 ℃), avoid steam to enter accumulator tank and cause waste, improve the thermal efficiency.
4, the utility model utilizes superconducting liquid-vapor to be expanded to power, need not outside resources, reaches self circulation, reduces cost.
Description of drawings
Fig. 1 is the utility model overall structure schematic diagram;
Fig. 2 is the structural representation of heat exchanger in the utility model.
The specific embodiment
Below in conjunction with accompanying drawing structure of the present utility model is described in further details.
Referring to Fig. 1, the utility model provides a kind of closed energy-saving heating heat-exchange system, comprise decompressor 1, radiator 2, accumulator tank 3, be provided with heat exchanger 4 between described decompressor 1 and the radiator 2, be provided with temperature control valve 5 between heat exchanger 4 and the accumulator tank 3, be provided with hot and cold water heat exchange box 6 between temperature control valve 5 and the accumulator tank 3.
Referring to Fig. 2, the heat dump 7 in the utility model in the heat exchanger 4 is the pawl type, makes the heat exchange liquid 8 of filling between heat exchanger 4 and the heat dump 7 big with heat dump 7 contacts area, and it is effective to be heated, and the heat exchange liquid 8 of filling between heat exchanger 4 and the heat dump 7 is superconducting fluid.
During work, utilize the steam decompressor that high steam is depressured to 0.4MPa, temperature is 143 ℃, as the heat exchange thermal source, after the superconducting fluid in the heat exchanger was heated, liquid state became the mist attitude, speed with 27～30m/s begins to propagate, release heat is on the way carried out heat release through fin to indoor, and temperature control reaches the indoor heating requirement.Condensed water in the heat exchanger after the heat exchange enters accumulator tank through temperature control valve, temperature control valve control temperature is at 80 ℃, when being lower than serviceability temperature, temperature in jar, exits for 70 ℃～80 ℃, stop venting when being higher than 70 ℃～80 ℃, thereby reduce the steam use amount more than 60%, save cost, improved steam utilization.Can build the boiler room in place with good conditionsi, the hot and cold water heat exchange box of the condensed water after the heat exchange in temperature control valve enters the boiler room, boiler is heated into steam with water, can be recycling, perhaps be used in the place that other need use steam.
Claims (4)
1, a kind of closed energy-saving heating heat-exchange system comprises decompressor, radiator, accumulator tank, it is characterized in that: be provided with heat exchanger between described decompressor and the radiator, be provided with temperature control valve between heat exchanger and the accumulator tank.
2, a kind of closed energy-saving heating heat-exchange system according to claim 1 is characterized in that: be provided with the hot and cold water heat exchange box between said temperature control valve and the accumulator tank.
3, a kind of closed energy-saving heating heat-exchange system according to claim 1 is characterized in that: the heat dump in the above heat exchanger is the pawl type.
4, a kind of closed energy-saving heating heat-exchange system according to claim 1 is characterized in that: the heat exchange liquid of filling between the above heat exchanger and the heat dump is superconducting fluid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200803857U CN201215351Y (en) | 2008-05-08 | 2008-05-08 | Closed type energy-conserving heating and heat exchanging system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200803857U CN201215351Y (en) | 2008-05-08 | 2008-05-08 | Closed type energy-conserving heating and heat exchanging system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201215351Y true CN201215351Y (en) | 2009-04-01 |
Family
ID=40520556
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200803857U Expired - Fee Related CN201215351Y (en) | 2008-05-08 | 2008-05-08 | Closed type energy-conserving heating and heat exchanging system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201215351Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101270895B (en) * | 2008-05-08 | 2010-06-16 | 北京敦华石油技术有限公司 | Closed energy-saving heating heat-exchange system |
-
2008
- 2008-05-08 CN CNU2008200803857U patent/CN201215351Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101270895B (en) * | 2008-05-08 | 2010-06-16 | 北京敦华石油技术有限公司 | Closed energy-saving heating heat-exchange system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: XINJIANG DUNHUA PETROLEUM TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: BEIJING DUNHUA PETROLEUM TECHNOLOGY CO., LTD. Effective date: 20100115 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20100115 Address after: Room 5, building 1256, No. 830011, Hebei East Road, the Xinjiang Uygur Autonomous Region, Urumqi, China: B1 Patentee after: Xingjiang Dunhua Petroleum Technology Co., Ltd. Address before: Beijing City, Chaoyang District Yumin Road A China international science and Technology Exhibition Center No. 12, block 1705, zip code: 100029 Patentee before: Beijing Dunhua Petroleum Technology Co., Ltd. |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090401 Termination date: 20130508 |