SU532725A1 - Steam and gas heating system - Google Patents
Steam and gas heating systemInfo
- Publication number
- SU532725A1 SU532725A1 SU2101558A SU2101558A SU532725A1 SU 532725 A1 SU532725 A1 SU 532725A1 SU 2101558 A SU2101558 A SU 2101558A SU 2101558 A SU2101558 A SU 2101558A SU 532725 A1 SU532725 A1 SU 532725A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- steam
- heating system
- gas heating
- boiler
- gas
- Prior art date
Links
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- Air Supply (AREA)
Description
1one
Изобретение относитс к системам парогазового отоплени и может быть использовано при отоплении промышленных, общесвенных и жилых зданий.The invention relates to gas-vapor heating systems and can be used for heating industrial, public and residential buildings.
Известна система парогазового отоплени 1J , в которой теплоносителем вл етс смесь вод ного пара с продуктами сгорани топлива. Смесеобразование происходит в генераторе тепла. Побудителем движени теплоносител вл етс электроэнерги , затрачиваема в компрессорах дл подачи воздуха. Дополнительно к котельной требуетс сооружение компрессорной. СтоимостьA known steam gas heating system 1J, in which the coolant is a mixture of water vapor and fuel combustion products. Mixing occurs in the heat generator. The driving force behind the coolant is the electrical energy consumed in the compressors to supply air. In addition to the boiler room, the construction of a compressor is required. Cost of
электроэнергии намного превышает стоимость сэкономленного газа.electricity far exceeds the cost of gas saved.
Известна система парогазового отоплений , в которой смешение вод ного пара с воздухом происходит в паровом эжекторе. Побудителем движени в системе вл етс энерги пара, поступающего из генератора. Система включает паровой котел, эжектор, питаемый от котла, и засасываюший воздух, разделитель конденсата и газов, конденсатный бак и трубопроводы.A steam-gas heating system is known, in which the mixing of water vapor with air takes place in a steam ejector. The driving force in the system is the energy of steam coming from the generator. The system includes a steam boiler, an ejector fed from the boiler and suction air, a separator for condensate and gases, a condensate tank and pipelines.
При этом вод на часть разделител соединена с конденсатным баком а воздушна - с эжектором. Газопроводы дл удалени дымовых газов от котла введены непосредственно в дымовую трубку 2, Система характеризуетс р дом достоинств, однако имеет р д недостатков.In this case, the water to the part of the separator is connected to the condensate tank and the air to the ejector. Pipelines for removing flue gases from the boiler are introduced directly into flue pipe 2. The system is characterized by a number of advantages, however, it has several disadvantages.
Газопроводы дл удалени продуктов сгорани от котла введены непосредственно в дымовую трубу. Из-за этого продукты сгорани унос т в атмосферу свое тепло, а также воду, образовавшуюс при сгораш и топлива . Вод на часть разделител соединена с конденсатным баком, Вода поступает в бак, а затем в котел с пониженной .смпературой , это требует затраты на ее подогрев до начала парообразовани .Pipelines to remove combustion products from the boiler are introduced directly into the chimney. Because of this, the products of the combustion carry away their heat to the atmosphere, as well as the water formed during the combustion and fuel. Water is partly connected to the condensate tank, Water enters the tank and then into the boiler with a reduced temperature, this requires the cost of heating it before steam generation begins.
Цель изобретени - обеспечение экономии топлива.The purpose of the invention is to provide fuel economy.
Дл этого система снабжена скруббером, через который трубопроводы соединены с эжекторами, а разделитель газов и Конденсата своей водной частью св зан со скруббером , а газовой - с дымовой трубой.For this, the system is equipped with a scrubber, through which the pipelines are connected to the ejectors, and the gas separator and the Condensate are connected to the scrubber by their water part, and the gas pipe to the stack.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU2101558A SU532725A1 (en) | 1975-02-03 | 1975-02-03 | Steam and gas heating system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU2101558A SU532725A1 (en) | 1975-02-03 | 1975-02-03 | Steam and gas heating system |
Publications (1)
Publication Number | Publication Date |
---|---|
SU532725A1 true SU532725A1 (en) | 1976-10-25 |
Family
ID=20608945
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU2101558A SU532725A1 (en) | 1975-02-03 | 1975-02-03 | Steam and gas heating system |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU532725A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120248213A1 (en) * | 2010-07-30 | 2012-10-04 | Robert Kremer | Hyper-Condensate Recycler |
-
1975
- 1975-02-03 SU SU2101558A patent/SU532725A1/en active
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120248213A1 (en) * | 2010-07-30 | 2012-10-04 | Robert Kremer | Hyper-Condensate Recycler |
US8936202B2 (en) * | 2010-07-30 | 2015-01-20 | Consolidated Edison Company Of New York, Inc. | Hyper-condensate recycler |
US20150192308A1 (en) * | 2010-07-30 | 2015-07-09 | Robert Kremer | Hyper-condensate recycler |
US9506659B2 (en) * | 2010-07-30 | 2016-11-29 | Robert Kremer | Hyper-condensate recycler |
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