SU532725A1 - Steam and gas heating system - Google Patents

Steam and gas heating system

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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
Application number
SU2101558A
Other languages
Russian (ru)
Inventor
Моисей Исаевич Фельдман
Леонид Михайлович Оноре-Артынов
Original Assignee
Государственный Республиканский Институт По Проектированию Газоснабжения И Комплексного Благоустройства Городов И Поселков
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Государственный Республиканский Институт По Проектированию Газоснабжения И Комплексного Благоустройства Городов И Поселков filed Critical Государственный Республиканский Институт По Проектированию Газоснабжения И Комплексного Благоустройства Городов И Поселков
Priority to SU2101558A priority Critical patent/SU532725A1/en
Application granted granted Critical
Publication of SU532725A1 publication Critical patent/SU532725A1/en

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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.

SU2101558A 1975-02-03 1975-02-03 Steam and gas heating system SU532725A1 (en)

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

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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)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120248213A1 (en) * 2010-07-30 2012-10-04 Robert Kremer Hyper-Condensate Recycler

Cited By (4)

* Cited by examiner, † Cited by third party
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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