PL104403B1 - THE WAY OF RECOVERING WASTE HEAT - Google Patents
THE WAY OF RECOVERING WASTE HEAT Download PDFInfo
- Publication number
- PL104403B1 PL104403B1 PL19053276A PL19053276A PL104403B1 PL 104403 B1 PL104403 B1 PL 104403B1 PL 19053276 A PL19053276 A PL 19053276A PL 19053276 A PL19053276 A PL 19053276A PL 104403 B1 PL104403 B1 PL 104403B1
- Authority
- PL
- Poland
- Prior art keywords
- heat
- methane
- waste heat
- furnace
- recovering waste
- Prior art date
Links
- 239000002918 waste heat Substances 0.000 title claims description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 24
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 239000003546 flue gas Substances 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 3
- 239000003345 natural gas Substances 0.000 claims description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 2
- 238000011084 recovery Methods 0.000 description 4
- 239000000567 combustion gas Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 244000144980 herd Species 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
Przedmiotem wynalazku jest sposób odzysku ciepla odpadowego, traconego uchodzeniem do atmosfery gazów spalinowych, wytwarzajacych sie w piecach przemyslowych, zwlaszcza opalanych gazem ziemnym, czyli sposób zmniejszania tak zwanej straty kominowej. Wynalazek przeznaczony jest do stosowania zwlaszcza w przemysle szklar¬ skim ii iw hutnictwie* Znane sposoby odzysku ciepla odpadowego, tra¬ conego uchodzeniem do atmosfery goracych gazów spalinowych, wytwarzajacych sie w piecach prze¬ myslowych, polega na podgrzewaniu tymi goracymi spalinami przed ich ujsciem do atmosfery wsadu piecowego, wzglednie powietrza pierwotnego i/lub wtórnego, potrzebnego dla prawidlowego przebiegu procesu spailania, czyli odzysku czesci ciepla fizycz¬ nego. Urzadzenia w których gorace spaliny oddaja czesc ciepla odpadowego wsadowi piecowemu, wzglednie powietrzu pierwotnemu i/lub wtórnemu, nazywaja sie wymiennikami ciepla, wsród których rozróznia sie regeneratory pracujace okresowo i re- kuperatury pracujace w sposób ciagly.The subject of the invention is a recovery method waste heat, lost from escaping to flue gas generating atmosphere in industrial furnaces, especially fired natural gas, i.e. the way to reduce yes known as the stack loss. The invention is intended it is particularly suitable for use in the glass industry skim ii and in metallurgy * Known methods of waste heat recovery, waste heat due to the escape of hot gases into the atmosphere combustion gases produced in combustion furnaces thinking, is to heat the hot ones flue gas prior to their escape to the charge atmosphere furnace or primary air and / or necessary for proper mileage the process of burning, i.e. the recovery of some physical heat one. Devices in which they give off hot exhaust fumes part of the waste heat in the furnace charge, relatively primary and / or secondary air, they are called heat exchangers, among which a distinction is made between regenerators operating periodically and re- continuously operating cuperatures.
(Wada znanych sposobów odzysku ciepla odpado¬ wego jest to, ze niezaleznie od rodzaju urzadzen, wymiana ciepla nastepuje przez przenikanie ciepla ze spalin do wsadu piecowego i/lub do powietrza, wzglednie przez przenikanie ciepla ze spalin do elementów urzadzen, a nastepnie przez promienio¬ wanie ciepla z tych elementów do wsadu pieco- 2 wego i/lub1 powietrza. W kazdym z tych przypad¬ ków jest to tylko cieplo fizyczne.(A disadvantage of the known heat recovery processes is omitted what is important is that, regardless of the type of device, heat exchange occurs through heat transfer from the flue gas to the furnace charge and / or to the air, relatively by heat transfer from the flue gas to components of devices and then through the beam transferring heat from these elements to the furnace charge 2 air and / or air. In either case it is only physical heat.
Istota wynalazku polega na wykorzystaniu ciepla gazów spalinowych, wytwarzajacych sie w piecu przemyslowym, do endotermicznej reakcji konwer¬ sji metanu z para wodna, przy czym mieszanine metanu i pary wodnej w .stosunku wagowym CH4 : H^O najkorzystniej 16 : 18, ogrzewa sie do temperatury powyzej 950°K cieplem gazów odcho¬ dzacych z komory reakcyjnej pieca. Nowo powstala mieszanine gazowa tlenku wegla i wodoru wpro¬ wadza sie nastepnie do spalania w komorze reak¬ cyjnej pieca.The essence of the invention is the use of heat the combustion gases produced in the furnace industrial, for endothermic converter reaction the separation of methane from steam, the mixture being a mixture methane and water vapor in the weight ratio CH 4: H 2 O, most preferably 16:18, warmed to temperatures above 950 ° K with the heat of the gases deviating running out of the reaction chamber of the furnace. Newly established a gas mixture of carbon monoxide and hydrogen was introduced it is then put into combustion in the reaction chamber of the furnace.
[Zaleta sposobu wedlug wynalazku jest to, ze otrzymana w wyniku absorbujacej cieplo reakcji konwersji metanu z para wodna mieszanina tlenku wegla i wolnego wodoru ma o okolo 2i5tyo(wiekJsiza kalorycznosc niz zuzyty na wytworzenie tej mie¬ szaniny metan.[An advantage of the method of the invention is that obtained by a heat-absorbing reaction converting methane from water vapor to an oxide mixture carbon and free hydrogen is about 2.500 (the age ofJsiza calorific value than used in the production of this city methane gas.
Praktyczny przyklad wykorzystania wynalazku pokazany jest i omówiony na jednym z wielu moz¬ liwych ukladów, na rysunku przedstawiajacym schemat ukladu.A practical example of using the invention is shown and discussed in one of the many pictures live circuits in the figure showing layout diagram.
Przyklad. Gazy spalinowe, wytwarzajace sie w piecu 1 szklarskim, opalanym gazem ziemnym, posiadajace temperature powyzej 1!2J00°K kieruje sie czesciowo do konwertora 2, w którym metan reaguje w temperaturze powyzej 55»0oK z para wodna, doprowadzajab do zamiany CH4 + H20 + + q = 00 + 3H2, a czesciowo do jednego z rege- 104 403104 403 rieratorów 3, a w nastepnej kolejnosci do kotla pa¬ rowego 4 i dopiero stad o temperaturze okolo 400°iK do atmosfery. W tym czasie piec 1 zasilany jest mieszanina z konwertora 2 i powietrzem na¬ grzanym w drugim regeneratorze 5. Po pewnymi okresie gorace gazy spalinowe kieruje sie z pieca X do konwertora 2 i do regeneratora 5 i wówczas piec 1 izasila sie powietrzem nagrzanym w regene¬ ratorze 3. Ilosc metanu do pary wodnej wynosi 16 czesci wagowych metanu do 18 czesci wago¬ wych ipary wodnej. 4 > woda LZGraf. Z-d Nr 2 — H224/79 100 egz. A-4 Cena 45 zlExample. Exhaust gases, producing in 1 glass furnace, fired with natural gas, having a temperature above 1! 2J00 ° K drives partially to converter 2, in which methane reacts at temperatures above 55 ° C with steam water, lead to CH4 + H20 + conversion + q = 00 + 3H2, and partially to one of the regions 104 403 104 403 rieratorów 3, and then to the boiler trench 4 and only herds with a temperature of approx 400 ° iK to the atmosphere. At this time, furnace 1 energized there is a mixture of converter 2 and air to heated in the second regenerator 5. After certain period, the hot exhaust gases are directed from the furnace X to converter 2 and to regenerator 5 and then furnace 1 is supplied with air heated in regene ratorze 3. The amount of methane to water vapor is 16 parts by weight of methane to 18 parts by weight water vapor. 4> water LZGraf. Z-d No. 2 - H224 / 79 100 copies A-4 Price PLN 45
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL19053276A PL104403B1 (en) | 1976-06-18 | 1976-06-18 | THE WAY OF RECOVERING WASTE HEAT |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL19053276A PL104403B1 (en) | 1976-06-18 | 1976-06-18 | THE WAY OF RECOVERING WASTE HEAT |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL104403B1 true PL104403B1 (en) | 1979-08-31 |
Family
ID=19977375
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL19053276A PL104403B1 (en) | 1976-06-18 | 1976-06-18 | THE WAY OF RECOVERING WASTE HEAT |
Country Status (1)
| Country | Link |
|---|---|
| PL (1) | PL104403B1 (en) |
-
1976
- 1976-06-18 PL PL19053276A patent/PL104403B1/en unknown
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