CN1843580A - Circulating slurry sprinkling device for desulfurization of flue gas - Google Patents
Circulating slurry sprinkling device for desulfurization of flue gas Download PDFInfo
- Publication number
- CN1843580A CN1843580A CN 200610200288 CN200610200288A CN1843580A CN 1843580 A CN1843580 A CN 1843580A CN 200610200288 CN200610200288 CN 200610200288 CN 200610200288 A CN200610200288 A CN 200610200288A CN 1843580 A CN1843580 A CN 1843580A
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- CN
- China
- Prior art keywords
- spray
- flue gas
- desulfurization
- sprinkling device
- circulating slurry
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- Legal status (The legal status 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 status listed.)
- Granted
Links
- 239000002002 slurry Substances 0.000 title claims abstract description 46
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 24
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims description 23
- 239000003546 flue gas Substances 0.000 title claims description 23
- 230000023556 desulfurization Effects 0.000 title claims description 16
- 239000007921 spray Substances 0.000 claims abstract description 89
- 238000010521 absorption reaction Methods 0.000 claims description 39
- 238000005507 spraying Methods 0.000 claims description 17
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 10
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 10
- 239000011152 fibreglass Substances 0.000 claims description 7
- 230000007797 corrosion Effects 0.000 claims description 5
- 238000005260 corrosion Methods 0.000 claims description 5
- -1 polytetrafluoroethylene Polymers 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 3
- 238000003466 welding Methods 0.000 claims description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract description 8
- 239000000779 smoke Substances 0.000 abstract description 7
- 238000001179 sorption measurement Methods 0.000 abstract description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract description 4
- 235000019738 Limestone Nutrition 0.000 abstract description 4
- 235000011941 Tilia x europaea Nutrition 0.000 abstract description 4
- 239000004571 lime Substances 0.000 abstract description 4
- 239000006028 limestone Substances 0.000 abstract description 4
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 2
- 238000005299 abrasion Methods 0.000 abstract 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 229910000851 Alloy steel Inorganic materials 0.000 description 3
- 239000003517 fume Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000010440 gypsum Substances 0.000 description 3
- 229910052602 gypsum Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 210000002966 serum Anatomy 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 208000033999 Device damage Diseases 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000011440 grout Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- HUAUNKAZQWMVFY-UHFFFAOYSA-M sodium;oxocalcium;hydroxide Chemical compound [OH-].[Na+].[Ca]=O HUAUNKAZQWMVFY-UHFFFAOYSA-M 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The invention relates to a smoke desulfuration cycle slurry spray device, which are layered in the adsorption tower. Each spray device is formed by at least two parallel spray main tube and the spray sub tubes branched from the spray main tube. The dual-direction ejectors that branched from the spray sub tubes are interlaced into mesh spray layer; two parallel spray main tubes are through the hole of support beam inside the adsorption tower, and horizontally fixed via single-beam support. The invention can solve the problems that not enough mixed between the smoke and cycle slurry; lower desulfuration effect; and easy abrasion and leakage at the interface between the spray tubes and the adsorption tower. The invention can be used in wet smoke desulfuration adsorption tower to utilize the limestone or lime slurry to adsorb the sulfur dioxide and sulfur trioxide.
Description
(1) technical field
The present invention relates to a kind of circulating slurry sprinkling device that uses at the limestone/lime wet method fume desulfurizing system.
(2) background technology
Most power plant of China and industrial boiler adopt coal, wet goods fossil fuel usually, because the fossil fuel source is unstable, quality is unstable, sulfur content is higher, can produce harmful substances such as a large amount of sulfur dioxide in combustion process.In order to remove the sulfur dioxide in power plant, the boiler smoke, be extensive use of the limestone-gypsum wet flue gas desulfurization absorption tower in the large-sized station boiler, one of most important equipment is a spray equipment in the absorption tower.The tradition spray equipment generally is welded on the absorption tower inwall, mainly is made up of the steel alloy shower of costliness, is connected with unidirectional nozzle on the steel alloy shower.Because the shower irrational distribution, the shower internal pressure is unbalanced, the grout distribution inequality that sprays out, and slurries easily precipitate, utilization rate is not high.Some sulfur-containing smoke gas can not get abundant spray, and flue gas can not fully mix with loop slurry, and it is unclean that sulphur content is removed, and desulfuration efficiency remains further to be improved.For reaching clean cigarette purpose, must increase sprinkling equipment or increase spray time, the power consumption of recycle slurry liquid pump is significantly improved.In addition, wearing and tearing take place and reveal in traditional spray piping and absorption tower interface easily.
(3) summary of the invention
The purpose of this invention is to provide the circulating slurry sprinkling device that a kind of fume desulfurating absorption tower uses, solve the problem that flue gas and loop slurry undercompounding, desulfuration efficiency remain further raising; And solve the problem that spray piping and absorption tower interface wear and tear easily and reveal.
Technical scheme of the present invention: this circulating slurry sprinkling device for desulfurization of flue gas, layering setting in the absorption tower, it is characterized in that: every layer of spray equipment by at least two parallel sprays be responsible for, from spray be responsible for the spray arm of telling, the two-way nozzle of telling from spray arm both sides is woven into netted spraying layer, the perforate that two parallel sprays are responsible for to pass the brace summer absorption tower in, by the single-beam support, above-mentioned brace summer horizontal fixed is in the absorption tower.
Welding has the interface tube of ring flange on the above-mentioned absorption tower, and the spray person in charge passes this interface tube and stretches in the absorption tower.
Above-mentioned spray is responsible for brace summer perforate contact position, at absorption tower and interface tube contact position pad polytetrafluoroethylene (PTFE) backing plate.
Above-mentioned spray is responsible for and the spray arm is lined with the glass reinforced plastic pipe of wear-and corrosion-resistant layer inside and outside being.
The diameter that above-mentioned spray is responsible for dwindles gradually from near-end to far-end or stairstepping dwindles by joint.
The diameter of above-mentioned spray arm dwindles gradually from near-end to far-end or stairstepping dwindles by joint.
Said nozzle twines bonding with the spray arm by fiberglass cloth.
Said nozzle arrange density be 0.7-1.1 nozzle/square metre.
Said nozzle is a two-way nozzle up and down.
The end of above-mentioned spray arm places in the sliding support that absorbs the Tata wall.
The present invention is arranged in the flue gas desulfur device absorption tower, but arranging multiplayer, the sprayed slurry of using is the mixed serum of absorption tower stock tank sodalime stone slurries or lime slurry and gypsum, sprayed slurry is responsible for by spray and is flowed to the spray arm, flow to nozzle by the spray arm again, spray to the flue gas that flows with vaporific form from bottom to top.Its effect is that the mixed serum with lime stone and gypsum sprays in the flue gas with vaporific form, and flue gas is washed; Because the adsorption tower smoke flow velocity can be controlled in the 3-4m/s scope, the cigarette temperature can be controlled in the 50-100 ℃ of scope, and serum density is controlled at about 15%, and the pH value is controlled between the 5-6.Can realize the absorption of FGD absorption tower to sulfur dioxide after spraying into slurries with this understanding, desulfuration efficiency is the highest can to reach 90-98%.
Compare with the spray equipment of routine, the present invention has following beneficial effect:
1, energy consumption greatly reduces.Nozzle is hollow off-centre, two-way nozzle up and down, nozzle spray angle in 30-150 degree scope, each designs of nozzles flow be calculate separately according to each engineering different definite.Improved spraying intensity greatly, made liquid-gas ratio L/G (ratio of slurries internal circulating load and clean fume side volume flow) reduce by 5%, greatly reduced the power consumption of recycle slurry liquid pump than conventional spray equipment.Owing to can enable less spraying layer, can reach identical desulfuration efficiency, energy consumption reduces by 4%; 20% of the not enough alloy material spraying layer of gross investment cost.
2, construction is convenient, equipment is not fragile.The support structure designs of spraying layer of the present invention is reasonable, the support that spray is responsible for adopts single-beam to support, middle perforate at brace summer, spray is responsible for and is passed from perforate, between pad polytetrafluoroethylene (PTFE) backing plate, guarantee that spraying layer can free wxpansion when variations in temperature, and can not cause excessive thrust the absorption tower wallboard.The thermal expansion phenomenon that the unexpected variation of temperature causes in the time of can satisfying unit and start fast, it is excessive can not thermal stress to take place, and causes the situation of device damage.The interface tube setting of flanged dish not only makes easy construction, quick, and working face is little, is convenient to processing and manufacturing and on-the-spot the installation; Wearing and tearing and leakage have also been prevented.
3, avoid the depositional phenomenon of pipe wear or generation loop slurry.Spraying layer adopts that spray is responsible for, the form of spray arm, and shower adopts the form of convergent, stable and balanced with the holding tube internal pressure.Shower adopts three-decker fiberglass to make, sprinkle density be 0.7-1.1 nozzle/square metre, the spray velocity in pipes design for uniform flow, guarantee slurries can be in managing the generation depositional phenomenon, the excessive wear phenomenon can not appear.
4, load adaptability strengthens, owing to adopted two-way nozzle, slurries two directions up and down spray simultaneously, reduce the collision polymerism of drop, improved total absorption area of slurries, actual motion shows, even load improves 5-10%, desulfuration efficiency greatly improves.
5, with low cost.Compare with the steel alloy shower that routine adopts, the present invention is owing to selected special glass steel material for use, the slurries spray adopts sintered sic to make with nozzle, nozzle adopts the winding bonding way to be connected with shower, overall weight and cost reduce greatly, investment has also obtained significantly reducing, and its spraying layer cost has only the less than 20% of alloy material.
The present invention is applied to wet flue gas desulfurization absorption tower, is used to utilize lime stone slurry or lime slurry to absorb sulfur in smoke and sulfur trioxide.
(4) description of drawings
Fig. 1 is a structural representation of the present invention.
Fig. 2 is that brace summer is responsible for the schematic diagram that is connected with spray.
Fig. 3 is the schematic diagram that the absorption tower is provided with interface tube.
Among the figure: 1-absorption tower, 2-spray are responsible for, 3-sprays arm, 4-nozzle, 5-brace summer, 6-interface tube, 7-polytetrafluoroethylene (PTFE) backing plate, 8-sliding support
(5) specific embodiment
Embodiment is referring to Fig. 1-3, this circulating slurry sprinkling device for desulfurization of flue gas is stratified and set in the absorption tower 1, every layer of spray equipment by two parallel sprays be responsible for 2, from spray be responsible for the spray arm of telling 3, the two-way nozzle of telling from spray arm both sides 4 is woven into netted spraying layer.
Two parallel sprays are responsible for 2 perforates of passing brace summer 5 absorption tower in, are supported by single-beam, and above-mentioned brace summer horizontal fixed is the stability that increases spraying layer in the absorption tower, and the end of spray arm 3 places in the sliding support 8 of absorption Tata wall.The support of spraying layer adopts single-beam to support, and in the middle perforate of brace summer, spray is responsible for and is passed from perforate.
Welding has the interface tube 6 of ring flange on the absorption tower, and the spray person in charge passes this interface tube and stretches in the absorption tower.
Spray is responsible for 2 with brace summer perforate contact position, at absorption tower and interface tube contact position pad polytetrafluoroethylene (PTFE) backing plate 7.
Spray be responsible for 2 and spray arm 3 be lined with the glass reinforced plastic pipe of wear-and corrosion-resistant layer inside and outside being, can adopt triplex glass steel material to make, to prevent the slurries corrosion pipeline.The diameter of the spray person in charge and spray arm dwindles gradually from near-end to far-end or stairstepping dwindles by joint.
Nozzle 4 is sintered sics, and nozzle twines bonding with the spray arm for fiberglass cloth.Along with the variation of exhaust gas volumn, correspondingly open all or part of spraying layer.Nozzle is evenly arranged on the section of whole absorption tower, arrangement of nozzles density be 0.7-1.1 nozzle/square metre.Nozzle is hollow off-centre, two-way nozzle up and down, and the angle that the ejection slurries form is the 30-150 degree, and the best is 120 degree.Each designs of nozzles flow is to determine according to different calculating separately of each engineering.
For providing sprayed slurry to spray equipment, every layer of spraying layer is provided with a spray pump, extracts slurries in the spray pump self-absorption tower stock tank, slurries after boosting by spray equipment, by the spray person in charge-spray arm-nozzle, spray up and down with 120 degree angle taper shapes, spray into flue gas.Nozzle entrance slurries pressure is 0.7bar.For preventing spray nozzle clogging, at the spray pump inlet duct filter screen is set, to existing absorption tower, filter screen is installed on the spray pump entrance pipe, and to newly-built absorption tower, filter screen can be installed in the absorption tower.Consider that slurry pH value is 5-6, Cl
-The about 20000PPM of concentration, the material of spray pump is selected need take into account wear-resisting simultaneously and the acid corrosion-resistant requirement.
Every layer of spraying layer is provided with independent slurry circulating pump, and the slurry circulating pump inlet is installed independently filter screen and Shuttoff Valve, guarantees that every layer of spraying layer can turn-off separately.
Claims (10)
1. circulating slurry sprinkling device for desulfurization of flue gas, layering setting in the absorption tower, it is characterized in that: every layer of spray equipment by at least two parallel sprays be responsible for, from spray be responsible for the spray arm of telling, the two-way nozzle of telling from spray arm both sides is woven into netted spraying layer, the perforate that two parallel sprays are responsible for to pass the brace summer absorption tower in, by the single-beam support, above-mentioned brace summer horizontal fixed is in the absorption tower.
2. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 is characterized in that: welding has the interface tube of ring flange on the above-mentioned absorption tower, and the spray person in charge passes this interface tube and stretches in the absorption tower.
3. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: above-mentioned spray is responsible for brace summer perforate contact position, at absorption tower and interface tube contact position pad polytetrafluoroethylene (PTFE) backing plate.
4. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: above-mentioned spray is responsible for and the spray arm is lined with the glass reinforced plastic pipe of wear-and corrosion-resistant layer inside and outside being.
5. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: the diameter that above-mentioned spray is responsible for dwindles gradually from near-end to far-end or stairstepping dwindles by joint.
6. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: the diameter of above-mentioned spray arm dwindles gradually from near-end to far-end or stairstepping dwindles by joint.
7. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: said nozzle twines bonding with the spray arm by fiberglass cloth.
8. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: said nozzle arrange density be 0.7-1.1 nozzle/square metre.
9. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: said nozzle is two-way nozzle up and down.
10. circulating slurry sprinkling device for desulfurization of flue gas according to claim 1 and 2 is characterized in that: the end of above-mentioned spray arm places in the sliding support that absorbs the Tata wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006102002882A CN100450587C (en) | 2006-03-30 | 2006-03-30 | Circulating slurry sprinkling device for desulfurization of flue gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006102002882A CN100450587C (en) | 2006-03-30 | 2006-03-30 | Circulating slurry sprinkling device for desulfurization of flue gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1843580A true CN1843580A (en) | 2006-10-11 |
| CN100450587C CN100450587C (en) | 2009-01-14 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006102002882A Active CN100450587C (en) | 2006-03-30 | 2006-03-30 | Circulating slurry sprinkling device for desulfurization of flue gas |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103537186A (en) * | 2013-11-07 | 2014-01-29 | 北京国能中电节能环保技术有限责任公司 | Desulphurization absorption tower |
| CN104857836A (en) * | 2015-05-12 | 2015-08-26 | 浙江天地环保工程有限公司 | Flue gas desulfurization absorber interactive spray system |
| CN105169915A (en) * | 2015-09-18 | 2015-12-23 | 江苏华星电力环保设备有限公司 | Novel desulphurization absorption tower |
| CN106362575A (en) * | 2016-08-27 | 2017-02-01 | 华润电力（菏泽）有限公司 | Desulfurization spraying system of thermal power plant, and desulfurization control method |
| CN107569997A (en) * | 2017-08-23 | 2018-01-12 | 河北可利尔环保设备有限公司 | A kind of absorption tower slurries spray equipment for power plant's wet desulphurization |
| CN108709034A (en) * | 2018-07-26 | 2018-10-26 | 大唐环境产业集团股份有限公司 | The attachment device of desulfurization sprayed slurry pipeline |
| CN108830024A (en) * | 2018-08-10 | 2018-11-16 | 山东电力工程咨询院有限公司 | A kind of alloy spraying layer design method and device for wet method fume desulfurizing system |
| CN109316927A (en) * | 2018-11-09 | 2019-02-12 | 中国科学院过程工程研究所 | A kind of tapering type ozone uniform device and its arrangement in flue |
| CN111408259A (en) * | 2020-04-14 | 2020-07-14 | 大唐环境产业集团股份有限公司 | Novel pipeline supporting mode |
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| US5352421A (en) * | 1989-12-05 | 1994-10-04 | University Of Toronto Innovations Foundation | Method and apparatus for effecting gas-liquid contact |
| WO1996026785A1 (en) * | 1995-02-28 | 1996-09-06 | Babcock-Hitachi Kabushiki Kaisha | Wet type exhaust gas desulfurization method and apparatus utilizing solid desulfurizing agent |
| CN2376993Y (en) * | 1999-05-06 | 2000-05-10 | 彭铁成 | Integral flue gas desulfuration dust-collecting apparatus |
| CN2388999Y (en) * | 1999-09-09 | 2000-07-26 | 刘健民 | Wet method double water curtain desulfurating apparatus |
| CN2439901Y (en) * | 2000-09-06 | 2001-07-25 | 四川金海企业有限公司 | Two-circulation two-stage smoke desulfurizing tower |
| CN2452604Y (en) * | 2000-11-27 | 2001-10-10 | 唐念华 | Device for smoke-elliminating, sulphur-removing and dust-removing |
| CN2894805Y (en) * | 2006-03-30 | 2007-05-02 | 国电科技环保集团有限公司 | Flue gas desulfurizing circulating seriflux spraying apparatus |
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2006
- 2006-03-30 CN CNB2006102002882A patent/CN100450587C/en active Active
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|---|---|---|---|---|
| CN103537186A (en) * | 2013-11-07 | 2014-01-29 | 北京国能中电节能环保技术有限责任公司 | Desulphurization absorption tower |
| CN104857836A (en) * | 2015-05-12 | 2015-08-26 | 浙江天地环保工程有限公司 | Flue gas desulfurization absorber interactive spray system |
| CN105169915A (en) * | 2015-09-18 | 2015-12-23 | 江苏华星电力环保设备有限公司 | Novel desulphurization absorption tower |
| CN106362575A (en) * | 2016-08-27 | 2017-02-01 | 华润电力（菏泽）有限公司 | Desulfurization spraying system of thermal power plant, and desulfurization control method |
| CN106362575B (en) * | 2016-08-27 | 2019-07-09 | 华润电力（菏泽）有限公司 | A kind of heat-engine plant desulfurized spray system and method for controlling desulfurization |
| CN107569997A (en) * | 2017-08-23 | 2018-01-12 | 河北可利尔环保设备有限公司 | A kind of absorption tower slurries spray equipment for power plant's wet desulphurization |
| CN108709034A (en) * | 2018-07-26 | 2018-10-26 | 大唐环境产业集团股份有限公司 | The attachment device of desulfurization sprayed slurry pipeline |
| CN108830024A (en) * | 2018-08-10 | 2018-11-16 | 山东电力工程咨询院有限公司 | A kind of alloy spraying layer design method and device for wet method fume desulfurizing system |
| CN108830024B (en) * | 2018-08-10 | 2024-03-22 | 山东电力工程咨询院有限公司 | Alloy spray layer design method and device for wet flue gas desulfurization system |
| CN109316927A (en) * | 2018-11-09 | 2019-02-12 | 中国科学院过程工程研究所 | A kind of tapering type ozone uniform device and its arrangement in flue |
| CN111408259A (en) * | 2020-04-14 | 2020-07-14 | 大唐环境产业集团股份有限公司 | Novel pipeline supporting mode |
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Effective date of registration: 20081226 Address after: Beijing City, Xuanwu District Xuanwu street outside No. 28 Futuris building block A No. 1609 Patentee after: Guodian Longyuan Environment Protection Engrg. Co., Ltd., Beijing Address before: Beijing City, Xuanwu District Baiguang road two No. Patentee before: Guo Dian Technology Environment Protection Group Co., Ltd. |
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Effective date of registration: 20130619 Address after: 100052 Beijing City, Xuanwu District Xuanwu street outside No. 28 Futuris building block A No. 1609 Patentee after: Guodian Longyuan Environment Protection Engrg. Co., Ltd., Beijing Patentee after: Guodian New Energy Technology Institute Address before: 100052 Beijing City, Xuanwu District Xuanwu street outside No. 28 Futuris building block A No. 1609 Patentee before: Guodian Longyuan Environment Protection Engrg. Co., Ltd., Beijing |
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Address after: 100039 room 901, 9 / F, building 1, yard 16, West Fourth Ring Middle Road, Haidian District, Beijing Patentee after: Guoneng Longyuan environmental protection Co.,Ltd. Patentee after: GUODIAN NEW ENERGY TECHNOLOGY INSTITUTE Address before: 100052 Beijing City, Xuanwu District Xuanwu street outside No. 28 Futuris building block A No. 1609 Patentee before: BEIJING GUODIAN LONGYUAN ENVIRONMENTAL ENGINEERING Co.,Ltd. Patentee before: GUODIAN NEW ENERGY TECHNOLOGY INSTITUTE |
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| CP03 | Change of name, title or address |