CN1621745A - Bottoms combustion air preheater system and method of ethylene cracking furnace - Google Patents
Bottoms combustion air preheater system and method of ethylene cracking furnace Download PDFInfo
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- CN1621745A CN1621745A CNA2003101152696A CN200310115269A CN1621745A CN 1621745 A CN1621745 A CN 1621745A CN A2003101152696 A CNA2003101152696 A CN A2003101152696A CN 200310115269 A CN200310115269 A CN 200310115269A CN 1621745 A CN1621745 A CN 1621745A
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- preheater
- water
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- cooler
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- 238000000034 method Methods 0.000 title claims abstract description 25
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 title claims abstract description 13
- 239000005977 Ethylene Substances 0.000 title claims abstract description 13
- 238000005336 cracking Methods 0.000 title claims abstract description 13
- 238000002485 combustion reaction Methods 0.000 title claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 69
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 238000000197 pyrolysis Methods 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 17
- 238000013022 venting Methods 0.000 claims description 13
- 238000010791 quenching Methods 0.000 claims description 11
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 9
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 9
- 239000004571 lime Substances 0.000 claims description 9
- 230000000712 assembly Effects 0.000 claims description 6
- 238000000429 assembly Methods 0.000 claims description 6
- 230000000171 quenching effect Effects 0.000 claims description 5
- 238000007689 inspection Methods 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 7
- 239000002918 waste heat Substances 0.000 description 7
- 239000000446 fuel Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000000295 complement effect Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Gasification And Melting Of Waste (AREA)
Abstract
The present invention is air preheating system and method for bottom combustor in ethylene cracking furnace. Cold air may be preheated in preheater with low pressure blow-down steam after balance in plant side, circulating chilling water for cracking furnace and condensing effluent from plant side as heating medium. The present invention utilizes the latent energy of available apparatus with few increase in apparatus without need of automatic control system to result in obvious energy saving effect.
Description
Technical field
The present invention relates to the energy conserving system that a kind of waste heat that utilizes heat medium carries out air preheat, especially can utilize the lp venting steam after plant area's balance, or enter plant area's condensate liquid before the water treatment workshop, or the waste heat of the heat mediums such as chilled water (chw) of pyrolysis furnace self circulatory system comes the air of heating pyrolyze furnace bottom burner, and is energy-conservation with the Fuel Consumption that reduces pyrolysis furnace.
Background technology
People want to utilize the waste heat of plant area's thermal medium to carry out energy-saving design in technical field, for example adopt the flue gas of pyrolysis furnace to make heating source etc., need to increase the energy consumption equipment that adds, as air blast and air-introduced machine, booster water pump and other auxiliary equipment or the like, the while discharged flue gas has dust again and can cause a lot of inconvenience.Can we design such energy conserving system so:
1, the whole base burning devices that are suitable for the pyrolysis furnace stove group of ethylene plant are formed a closed or open energy conserving system;
2, the air-preheating energy-saving system need not be provided with automatic control system.If changing, external environment can automatically adjust or simple a little manual adjustments;
3, the air-preheating energy-saving system need not increase or seldom increase the normal operation that the energy consumption equipment that adds is kept its energy conserving system, but self potential that utilizes pyrolysis furnace system relevant devices is kept the normal operation of system, selected heat medium all is that general petrochemical factory is common, utilize the waste heat of these media, do not need to add in addition external heat source;
4, this system operating flexibility is big, requires system operational parameters not tight, causes heat medium what and the change that has or not as seasonality, and the change of plant area's technological parameter causes the change of heating medium flow, and this energy conserving system can both adapt to this variation well.
Above-mentioned some also can think the technical characterstic of the type energy conserving system design.
It is reported that the similar novel energy-saving method both at home and abroad that possesses above-mentioned technical characterstic has proved this point at present without any report by the retrieval to domestic and international interrelated data.
For this reason, the invention provides the Ethylene Cracking Furnace At Bottom of Burner System and Method of Air Preheater that satisfies above-mentioned specification requirement.
Summary of the invention
According to background technology, the object of the present invention is to provide the lp venting steam that can utilize after plant area's balance, or enter plant area's condensate liquid before the water treatment workshop, or the waste heat of the heat medium of pyrolysis furnace self circulatory system chilled water (chw) comes the air of heating pyrolyze furnace bottom burner, thereby reduces the pyrolysis furnace Fuel Consumption.
To achieve these goals, the present invention is achieved through the following technical solutions:
A kind of Ethylene Cracking Furnace At Bottom of Burner System and Method of Air Preheater, mainly by preheater (1), steam trap (11), drainage pump (12) or centrifugal pump (13) are formed, and its method comprises the following steps:
1, the lp venting steam (14) after plant area's balance is introduced preheater (1), preheater (1) is under the negative pressure duty works, and utilizes pyrolysis furnace combustion chamber draft surplus, suction ambient, cool air and enter preheater (1), enter burner after becoming hot-air, enter burner hearth again;
2, behind the steam trap (11) that the preheater (1) of the certain area of lp venting steam process and preheater design are complementary, the flow of lp venting steam can be regulated automatically according to the variation of environment temperature;
3, steam reliably can also be kept its operation through the parameter balanced design of system in steam self pressure after becoming condensate liquid, also can be transported to the female pipe of plant area's lime set (4) through drainage pump (12) or centrifugal pump (13);
4, for pyrolysis furnace stove group, a base burning device is equipped with a preheater (1) and a steam trap (11), or two base burning devices are equipped with a preheater and a steam trap.Every stove preheater (1) is connected in parallel, can be by lime set female pipe (4) shared drainage pumps (12) or centrifugal pump (13) after the parallel connection.
Owing to adopted technique scheme, the present invention to have following advantage and effect:
1, this energy conserving system of the present invention belongs to open system, does not increase outside resources consumption basically, and energy conserving system can be regulated automatically when external environment changed;
2, this energy conserving system of the present invention is used in chilled water (chw) or lime set is done in the circulatory system of heat medium, also can obviously save the fuel consumption of pyrolysis furnace, reduces the power consumption of chilled water (chw) air cooler, the power consumption when reducing the cold liquid of plant area and entering the water treatment workshop;
3, the condensate liquid of this energy conserving system of the present invention can be recycled to plant area water treatment workshop;
4, the present invention is simple, cheap at the device structure that the burner bottom is equipped with, and working service is repaired simple and easy, and energy-saving effect is remarkable, and entire equipment can not increase the attendant newly.
Description of drawings
Fig. 1 is the flow chart of energy conserving system technical scheme of the present invention
Fig. 2 is the flow chart of another embodiment of the present invention energy conserving system technical scheme
Fig. 3 is the flow chart of yet another embodiment of the invention energy conserving system technical scheme
Fig. 4 A is a preheater structure collectivity front elevational schematic of the present invention
Fig. 4 B is a preheater structure collectivity schematic side view of the present invention
Fig. 4 C is a preheater structure collectivity schematic top plan view of the present invention
Among the figure: 1-preheater, 11-steam trap, 12-drainage pump, 13-centrifugal pump, 14-lp venting steam, 21-cooler, 22-quenching water column, 23-chilling water pump, heat exchanger in the 24-original system, the high-order water pot of 31-, 32-booster water pump, the 33-cooler, the female pipe of 4-plant area lime set, 5-water treatment workshop, the 41-housing, 42-linkage path, 43-air inlet (water inlet) manifold assemblies, 44-return branch assembly, 45-forewarmer heat exchange tube, 46-inspection hatch
The specific embodiment
Illustrate by Fig. 1, a kind of Ethylene Cracking Furnace At Bottom of Burner System and Method of Air Preheater, mainly by preheater 1, steam trap 11, drainage pump 12 or centrifugal pump 13 are formed, and its method comprises the following steps:
1, the lp venting steam after plant area's balance 14 is introduced preheaters 1, preheater 1 is under the negative pressure duty works, and utilizes pyrolysis furnace combustion chamber draft surplus, and suction ambient, cool air and enter preheater 1 enters burner after becoming hot-air, enters burner hearth again;
2, behind the steam trap 11 that the preheater 1 of the certain area of lp venting steam process and preheater design are complementary, the flow of lp venting steam can be regulated automatically according to the variation of environment temperature;
3, steam reliably can also be kept its operation through the parameter balanced design of system in steam self pressure after becoming condensate liquid, also can be transported to the female pipe 4 of plant area's lime set through drainage pump 12 or centrifugal pump 13;
4, for pyrolysis furnace stove group, a base burning device is equipped with a preheater 1 and a steam trap 11, or two base burning devices are equipped with a preheater and a steam trap.Every stove preheater 1 is connected in parallel, can be by the female pipe of lime set 4 a shared drainage pump 12 or centrifugal pumps 13 after the parallel connection.
General ethylene plant all is provided with the female pipe of steam, as the female pipe of S1 steam (1kg/cm
2, 120 ℃), the female pipe of S3 steam (3.5kg/cm
2, 148 ℃ of 145 ∽), also have S11 etc.We select for use S3 steam to do the heat medium source.S3 steam is the vapour source that the ethylene plant is used as other equipment, and the steam of other pressure rating also is the vapour source as miscellaneous equipment.The different steam of these pressure is from the auxilliary pot steam manufacturing shop of plant area, and also some is to merge to the female pipe of steam of pressure rating separately from the steam that device is separated.
The consumption of steam is to determine behind plant area's moisture balance.We utilize lp venting steam to do the heat medium source of preheater, be the steam of the unnecessary emptying after plant area's balance, the energy conserving system that a certain amount of steam of directly drawing us and need from the upper shed of the female pipe of this kind steam during use enters us just can, through after the heat exchange of energy conserving system, steam becomes the water treatment workshop 5 that condensate liquid is got back to auxilliary pot again.
The technical program technical data:
Heating medium flow----(50～100) kg/H (every flow that preheater is required)
Heat medium pressure----is below the 0.4Mpa
Cold air temperature rise----(90～135) ℃ (average ambient temperature position ± 25 ℃)
Drainage pump extruding gas pressure---(3～5) kg/cm
2(the N of plant area
2Gas, instrument wind or steam)
Illustrated by Fig. 2, another embodiment of the present invention is to utilize the pyrolysis furnace recycled quench water to make the preheating energy-saving systems of heat medium, mainly by preheater 1, and cooler 21, quenching water column 22, chilling water pump 23, the heat exchanger 24 of original system, its method comprises the following steps:
1, locate before the cooler 21 in the pyrolysis furnace chilled water (chw) circulatory system, extension or whole recycled quench water are in air preheater 1;
2, before returning cooler 21 from preheater 1 outflow again after chilled water (chw) is lowered the temperature, behind cooler 21, get back to quenching water column 22 again;
3, the preheater 1 of pyrolysis furnace bottom is by the back method in parallel of connecting earlier, and the chilled water (chw) that will be lowered the temperature by the return main works on before being transmitted back to cooler 21 again.
Pyrolysis furnace stove group's cracking gas must be through chilled water (chw) cooling cutting out partial product, so chilled water (chw) obtains a part of heat of cracking gas and heats up.We utilize the part of waste heat of chilled water (chw) to heat air preheater, and generally the chilling water temperature of drawing before cooler is about 72 ℃, and pressure is about 8kg/cm
2∽ 10kg/cm
272 ℃ chilled water (chw) is lowered the temperature through behind the preheater, and the degree of cooling will be determined according to the flow size of used chilled water (chw) and the area of heat exchanger.Before being returned cooler by the chilled water (chw) of being lowered the temperature, the temperature of chilled water (chw) generally is controlled at 40 ℃ and enter quenching water column behind subcooler.This is a technological requirement, so the power save mode of the chilled water (chw) UTILIZATION OF VESIDUAL HEAT IN of the pyrolysis furnace circulatory system is a closed circulation system.
Make the pre-heating system technical data of heat medium with the pyrolysis furnace recycled quench water:
Heating medium flow----(0.5～15) T/H
Heat medium operating pressure----(3.5～10) kg/cm
2
72 ℃ of heat medium temperature----
Cold air temperature rise----(30～70) ℃ (average ambient temperature position ± 25 ℃)
Present embodiment has following advantage and effect:
1, present embodiment is the normal operation that pressure head more than needed when utilizing chilling water pump 23 design promotes chilled water (chw), at this moment is to utilize the potentiality of original equipment to move as seen.Utilize the waste heat of chilled water (chw) to heat burning and use cold air, saved the fuel consumption of pyrolysis furnace, lower the temperature owing to chilled water (chw) is preheated device that this has reduced the power consumption of cooler again simultaneously;
2, the present embodiment energy conserving system is a closed circulation system, and the drag losses of its drag losses and preheater all is very little.
Illustrated by Fig. 3, yet another embodiment of the invention is to utilize plant area's condensate liquid to make the preheating energy-saving systems of heat medium, mainly by preheater 1, and high-order water pot 31, booster water pump 32, cooler 33, plant area's condensate pipe 4, water treatment workshop 5, its method comprises the following steps:
1, plant area's condensate liquid at first is incorporated into high-order water pot 31 or be incorporated into booster pump 32 inlet to obtain pre-pressurized energy;
2, lime set is through preheater 1 heats cold air;
3, by the condensate liquid of being lowered the temperature get back to arrive cooler 33 again behind the return main before, get back to water treatment workshop 5 after lowering the temperature again.
Energy-conservation systems technology data when the preheating energy-saving systems of making heat medium with plant area's condensate liquid is made heat medium:
Required condensing water flow----(0.5～1.0) T/H (every preheater)
Advance preheater condensing water temperature----(120～150) ℃
Go out the preheater condensing water temperature---(60～80) ℃
Condensate water pressure----(3.5～4.0) kg/cm
2(gauge pressure)
Pre-pressurized energy----1kg/cm
2
The omnidistance pressure loss of condensate water is not more than 1kg/cm
2
Present embodiment has following advantage and effect:
1, present embodiment is an open-cycle system, and it has saved the fuel consumption of pyrolysis furnace and the power consumption of cooler;
2, the system of present embodiment composition is very simple, utilizes the member of original system mostly, and cheap for manufacturing cost, working service is repaired simple and easy.
By Fig. 4 A, 4B, 4C illustrates air preheater most crucial in the energy conserving system of the present invention 1, can be described as is to need the specialized designs manufacturing except that preheater 1 in energy conserving system, the miscellaneous equipment that relates in the system all is conventional basically, can on market, purchase, preheater 1 of the present invention, mainly by preheater shell 41, linkage path 42, air inlet (water inlet) manifold assemblies 43, return branch assembly 44, filter 45 is formed, wherein, preheater 1 is a square casing 41, its top is connected with the linkage path 42 with convergent contour cross section, at the interior arrangement of housing 41 forewarmer heat exchange tube 45 is arranged, on housing 41 1 sides, down and wherein device has air inlet (water inlet) manifold assemblies and return branch assembly, is provided with inspection hatch 46 at the opposite side of housing 41.
Preheater 1 is to be under the negative pressure state to work, and resistance is very little.It will design this preheater according to pyrolysis furnace condition of negative pressure and base burning device thermic load size.The effect of inspection hatch is the operating fifth wheel of cleaning, normally moves otherwise can influence preheater.
Air inlet wherein (water inlet) manifold assemblies comprises pipeline and on-off valve, filter etc., and the return branch assembly comprises on-off valve, drain valve etc.
When pressing in chilled water (chw) or plant area condensate liquid to be heat medium, do not need drain valve.
In a word, energy conserving system of the present invention, its novelty, creativeness, practicality are not increase or seldom increase and add under the energy consumption equipment prerequisite, rely on self potential of existing equipment to promote the normal operation of energy conserving system, do not need robot control system(RCS), working service is repaired simple and easy, energy-saving effect is obvious, operating flexibility is big, safeguards need not increase manpower newly, and it is the energy conserving system of the pyrolysis furnace of an independent and complete enclosed or open type.
Claims (4)
1, a kind of Ethylene Cracking Furnace At Bottom of Burner System and Method of Air Preheater, mainly by preheater (1), steam trap (11), drainage pump (12) or centrifugal pump (13) are formed, and its method comprises the following steps:
(1), the lp venting steam (14) after plant area's balance is introduced preheater (1), preheater (1) is under the negative pressure duty works, and utilizes pyrolysis furnace combustion chamber draft surplus, suction ambient, cool air and enter preheater (1), enter burner after becoming hot-air, enter burner hearth again;
(2), lp venting steam is through preheater (1) and the steam trap (11) of certain area, after preheater and steam trap running parameter are definite, the flow of lp venting steam will can be regulated automatically according to the variation of environment temperature;
(3), steam reliably can be kept its operation in steam self pressure after becoming condensate liquid, and can be transported to the female pipe of plant area's lime set (4) through drainage pump (12) or centrifugal pump (13);
(4), for pyrolysis furnace stove group, base burning device is equipped with a preheater (1) and a steam trap (11), every stove preheater (1) is connected in parallel, can be by female (4) shared drainage pumps (12) or the centrifugal pump (13) of managing of lime set after the parallel connection.
2, Ethylene Cracking Furnace At Bottom of Burner System and Method of Air Preheater according to claim 1 is characterized in that: utilize the pyrolysis furnace recycled quench water to make the pre-heating system and the method for heat medium, mainly by preheater
(1), cooler (21), quenching water column (22), chilling water pump (23), the heat exchanger of original system (24) is formed, and its method comprises the following steps:
(1), in the pyrolysis furnace chilled water (chw) circulatory system the preceding place of cooler (21), extension or all recycled quench water in air preheater (1);
(2), chilled water (chw) flows out that to return cooler (21) preceding after being lowered the temperature again from preheater (1), get back to quenching water column (22) behind cooler (21) again;
(3), the preheater (1) of pyrolysis furnace bottom is by series connection back method in parallel earlier, the chilled water (chw) that will be lowered the temperature by the return main is transmitted back to cooler (21) and works on before again.
3, Ethylene Cracking Furnace At Bottom of Burner System and Method of Air Preheater according to claim 1, it is characterized in that: utilize plant area's condensate liquid to make the pre-heating system and the method for heat medium, mainly by preheater (1), high-order water pot (31), booster water pump (32), cooler (33), plant area's condensate pipe (4), water treatment workshop (5) is formed, and its method comprises the following steps:
(1), plant area's condensate liquid at first is incorporated into high-order water pot (31) or be incorporated into booster pump (32) inlet to obtain pre-pressurized energy;
(2), condensate liquid is through preheater (1) heats cold air;
(3), enter cooler (33) after being got back to the return main by the condensate liquid of being lowered the temperature, get back to water treatment workshop (5) after the cooling again.
4, Ethylene Cracking Furnace At Bottom of Burner System and Method of Air Preheater according to claim 1, it is characterized in that: preheater (1) is mainly by preheater shell (41), linkage path (42), air inlet (water inlet) manifold assemblies (43), return branch assembly (44), forewarmer heat exchange tube (45) is formed, wherein, preheater (1) is square casing (41), its top is connected with the linkage path (42) with convergent contour cross section, interior arrangement at housing (41) has forewarmer heat exchange tube (45), on housing (41) one sides, down and wherein device has air inlet (water inlet) manifold assemblies and return branch assembly, is provided with inspection hatch (46) at the opposite side of housing (41).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101152696A CN100429461C (en) | 2003-11-27 | 2003-11-27 | Bottoms combustion air preheater system and method of ethylene cracking furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101152696A CN100429461C (en) | 2003-11-27 | 2003-11-27 | Bottoms combustion air preheater system and method of ethylene cracking furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1621745A true CN1621745A (en) | 2005-06-01 |
| CN100429461C CN100429461C (en) | 2008-10-29 |
Family
ID=34760370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2003101152696A Expired - Lifetime CN100429461C (en) | 2003-11-27 | 2003-11-27 | Bottoms combustion air preheater system and method of ethylene cracking furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100429461C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104197577A (en) * | 2014-09-03 | 2014-12-10 | 中国科学院理化技术研究所 | Refrigerating device driven by flue gas waste heat of ethylene cracking furnace |
| CN105467939A (en) * | 2014-09-04 | 2016-04-06 | 中国石油化工股份有限公司 | Optimization method for production and operation of ethylene cracking furnace |
| CN114993091A (en) * | 2022-05-18 | 2022-09-02 | 北京航化节能环保技术有限公司 | Zero-power-consumption self-adaptive distributed waste heat recycling system of ethylene device |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5865788A (en) * | 1981-10-14 | 1983-04-19 | Mitsui Eng & Shipbuild Co Ltd | Device for supplying preheated air |
| CN1033865A (en) * | 1987-12-31 | 1989-07-12 | 陆吉明 | Industrial Boiler condensate water and Steam Heating air method and preheater thereof |
| JPH11264535A (en) * | 1998-03-18 | 1999-09-28 | Nkk Corp | Method and device for controlling air temperature of steam air heater |
| GB2352803B (en) * | 1999-07-20 | 2001-07-25 | Foster Wheeler Energy Ltd | Air pre heater for fired process heater |
| RU2202072C2 (en) * | 2001-04-28 | 2003-04-10 | ОАО "Инжиниринговая компания "ЗиОМАР" | Multi-pass tubular air preheater |
-
2003
- 2003-11-27 CN CNB2003101152696A patent/CN100429461C/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104197577A (en) * | 2014-09-03 | 2014-12-10 | 中国科学院理化技术研究所 | Refrigerating device driven by flue gas waste heat of ethylene cracking furnace |
| CN105467939A (en) * | 2014-09-04 | 2016-04-06 | 中国石油化工股份有限公司 | Optimization method for production and operation of ethylene cracking furnace |
| CN105467939B (en) * | 2014-09-04 | 2018-04-10 | 中国石油化工股份有限公司 | A kind of optimization method of ethane cracking furnace production run |
| CN114993091A (en) * | 2022-05-18 | 2022-09-02 | 北京航化节能环保技术有限公司 | Zero-power-consumption self-adaptive distributed waste heat recycling system of ethylene device |
| WO2023221274A1 (en) * | 2022-05-18 | 2023-11-23 | 北京航化节能环保技术有限公司 | Zero-power-consumption adaptive distributed waste heat recycling system for ethylene plant |
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|---|---|
| CN100429461C (en) | 2008-10-29 |
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Assignee: Beijing Aerospace Petrochemical Technology and Equipment Engineering Corp. Assignor: BEIJING AEROSPACE PROPULSION INSTITUTE Contract fulfillment period: 2008.11.3 to 2013.11.2 Contract record no.: 2008110000176 Denomination of invention: Bottoms combustion air preheater system and method of ethylene cracking furnace Granted publication date: 20081029 License type: Exclusive license Record date: 20081208 |
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| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2008.11.3 TO 2013.11.2; CHANGE OF CONTRACT Name of requester: BEIJING SPACE PETROCHEMICAL TECHNOLOGY EQUIPMENT E Effective date: 20081208 |
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| C41 | Transfer of patent application or patent right or utility model | ||
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Effective date of registration: 20170120 Address after: 100076 Beijing, Fengtai District, South Road, No. 1, Patentee after: BEIJING AEROSPACE PETROCHEMICAL TECHNOLOGY & EQUIPMENT ENGINEERING Corp.,Ltd. Address before: 100076 Beijing, box 9200, box 11 Patentee before: Beijing Aerospace Propulsion Institute |
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| TR01 | Transfer of patent right |
Effective date of registration: 20170413 Address after: 100076 Beijing, Fengtai District, South Road, No. 1, Patentee after: Beijing wing wing Technology Co.,Ltd. Address before: 100076 Beijing, Fengtai District, South Road, No. 1, Patentee before: BEIJING AEROSPACE PETROCHEMICAL TECHNOLOGY & EQUIPMENT ENGINEERING Corp.,Ltd. |
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| TR01 | Transfer of patent right | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100076 Beijing, Fengtai District, South Road, No. 1, Patentee after: BEIJING HANGHUA ENERGY SAVING AND ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. Address before: 100076 Beijing, Fengtai District, South Road, No. 1, Patentee before: Beijing wing wing Technology Co.,Ltd. |
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| CX01 | Expiry of patent term |
Granted publication date: 20081029 |
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| CX01 | Expiry of patent term |