CN100560235C - Biogas residue drying and dehydration type municipal solid waste biological and incineration integrated process - Google Patents
Biogas residue drying and dehydration type municipal solid waste biological and incineration integrated process Download PDFInfo
- Publication number
- CN100560235C CN100560235C CNB2006100518641A CN200610051864A CN100560235C CN 100560235 C CN100560235 C CN 100560235C CN B2006100518641 A CNB2006100518641 A CN B2006100518641A CN 200610051864 A CN200610051864 A CN 200610051864A CN 100560235 C CN100560235 C CN 100560235C
- Authority
- CN
- China
- Prior art keywords
- incineration
- anaerobic fermentation
- recyclables
- incinerator
- sent
- Prior art date
- 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.)
- Expired - Fee Related
Links
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 29
- 238000001035 drying Methods 0.000 title claims abstract description 11
- 230000018044 dehydration Effects 0.000 title claims abstract description 7
- 238000006297 dehydration reaction Methods 0.000 title claims abstract description 7
- 238000000855 fermentation Methods 0.000 claims abstract description 44
- 239000005416 organic matter Substances 0.000 claims abstract description 19
- 239000000446 fuel Substances 0.000 claims abstract description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000003546 flue gas Substances 0.000 claims abstract description 6
- 238000000746 purification Methods 0.000 claims abstract 3
- 239000002893 slag Substances 0.000 claims description 21
- 239000007789 gas Substances 0.000 claims description 15
- 239000002918 waste heat Substances 0.000 claims description 8
- 239000010865 sewage Substances 0.000 claims description 7
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 6
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 6
- 241001330002 Bambuseae Species 0.000 claims description 6
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 6
- 239000011425 bamboo Substances 0.000 claims description 6
- 239000004566 building material Substances 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- 238000004332 deodorization Methods 0.000 claims description 4
- 239000002699 waste material Substances 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims 3
- 239000004753 textile Substances 0.000 claims 1
- 239000002023 wood Substances 0.000 claims 1
- 230000004151 fermentation Effects 0.000 abstract description 10
- 238000005516 engineering process Methods 0.000 abstract description 9
- 230000008901 benefit Effects 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 2
- 239000002002 slurry Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 description 12
- 239000010791 domestic waste Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 241000196324 Embryophyta Species 0.000 description 5
- 239000004744 fabric Substances 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 239000011449 brick Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 239000006148 magnetic separator Substances 0.000 description 4
- 239000004033 plastic Substances 0.000 description 4
- 229920003023 plastic Polymers 0.000 description 4
- 238000012216 screening Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- 239000002361 compost Substances 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- -1 stationery Substances 0.000 description 3
- 238000009264 composting Methods 0.000 description 2
- 239000013530 defoamer Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 239000008394 flocculating agent Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 230000007096 poisonous effect Effects 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
本发明涉及一种沼渣干燥脱水型城市生活垃圾生物与焚烧处理集成工艺。目前技术很难从根本上解决垃圾处理的现存问题。本发明的步骤是：破袋；分选；分选出的焚烧用可回收物送入焚烧炉进行焚烧处理，产生的烟气净化后达标排放；分选出的有机物和收集的垃圾渗沥液，送入厌氧发酵罐进行厌氧发酵生物处理，发酵产生的沼气经净化处理后用作燃料，发酵产生的沼渣干燥后送入焚烧炉焚化。本发明方法由于对沼渣干燥，使得沼液的达标处理非常容易；通过焚烧使得物料适应性强、二次污染少，可提升垃圾处理的效率和效益。The invention relates to an integrated biogas residue drying and dehydration type municipal solid waste biology and incineration treatment process. Current technology is difficult to fundamentally solve the existing problems of garbage disposal. The steps of the present invention are: bag breaking; sorting; the sorted recyclables for incineration are sent to the incinerator for incineration treatment, and the generated flue gas is purified and discharged up to the standard; the sorted organic matter and collected garbage leachate , sent to anaerobic fermentation tank for anaerobic fermentation biological treatment, the biogas produced by fermentation is used as fuel after purification, and the biogas residue produced by fermentation is dried and sent to incinerator for incineration. Because the method of the invention dries the biogas residue, it is very easy to treat the biogas slurry up to the standard; through incineration, the material has strong adaptability and less secondary pollution, and the efficiency and benefit of garbage treatment can be improved.
Description
Technical field
The present invention relates to a kind of urban garbage disposal technology, relate in particular to the biological and burning disposal integrated technique of a kind of dewatered city domestic garbage.
Background technology
Along with quickening of urbanization process, urban population quantity is constantly expanded, and the generation of domestic waste increases rapidly.Methods such as main at present technology of garbage disposal that adopts such as landfill, compost, burning, and anaerobic fermentation technology fails to popularize in developing country owing to reasons such as operation and construction cost height always.
Traditional garbage loading embeading is handled, and not only takies a large amount of soils, but also can produce as percolate the pollution of water body, the secondary pollutions such as landfill gas discharging in the landfill process.
Because China's rubbish is mixed collection, use the compost of producing without the house refuse of the pre-mixed collection that sorts, fertilizer efficiency is low, impurity is many, content of beary metal is high, cost is high, market outlet is poor, and not good to the treatment effects poisonous, harmful substance such as pathogen in the rubbish, can not make rubbish thoroughly innoxious.
Because moisture height, the calorific value of the primary domestic waste of China are low, directly adopt burning disposal technology, in order to promote fire box temperature, need to add a large amount of auxiliary fuels, auxiliary fuel consumes with station service power consumption rate all higher, and therefore hot income is not high, makes such enterprise relying on government subsidy too much.The direct burning of primary composting also can produce danger wastes such as poisonous lime-ash, particularly flying dust, and imperfect combustion product and noxious material content are higher in the tail gas, and surrounding environment is caused secondary pollution.In addition, excessive interpolation auxiliary fuel does not meet China's regenerative resource policy yet.
Anaerobic fermentation can produce valuable biogas, and secondary pollution is few, is favored by developed country always.But because the anaerobic fermentation cycle is long, it is big jar to hold, the compost deodorization is large-minded behind the fertile soil, station service is high, and natural pond slag mechanical dehydration need consume the flocculating agent and the defoamer of a large amount of costlinesses, the dehydration natural pond liquid processing cost of high COD is high, there is the market outlet problem too in its natural pond slag muck fertilizer, so in developing country the application achievement is arranged seldom.
Therefore, single technology of garbage disposal is difficult to fundamentally solve the existing problem of garbage disposal, and for the resource, minimizing, the innoxious target that realize garbage disposal, it is imperative to seek new trash processing way.
Summary of the invention
The objective of the invention is at the deficiencies in the prior art, a kind of treatment effeciency height, the little biological and integrated New Process for Treatment of burning of domestic waste of secondary pollution are provided.
The present invention comprises following steps and content:
Step 1: primary domestic waste is carried out broken bag.
Step 2: the rubbish after the broken bag is carried out physical separation, be divided into organic matter, inorganic matter, burning with Recyclable and recovery Recyclable.
Described burning comprises yarn fabric and wooden bamboo in the Recyclable with Recyclable, reclaims with Recyclable to comprise except that burning with all the other Recyclables the Recyclable.Recovery is directly carried out resource reutilization with Recyclable; Inorganic matter sanitary landfills or as the building materials raw material after collecting.
Step 3: with the burning Recyclable in the step 2, send into incinerator and carry out burning disposal, the incinerator fire box temperature is 800-950 ℃, and gas residence time is more than 2 seconds.The high-temperature flue gas that incinerator produces after waste heat recovery, qualified discharge after smoke eliminator purifies; The lime-ash that burn to produce sanitary landfills or as the building materials raw material after collecting.
Step 4: the organic matter in the step 2 is sent into anaerobic fermentation tank carry out the anaerobic fermentation of biological processing, fermentation temperature is 35-55 ℃.
Step 5: the biogas that the anaerobic fermentation in the step 4 produces is used as fuel after purified treatment; The natural pond slag that fermentation produces, the incinerator of sending into step 3 after the waste heat drying that utilization is reclaimed burns.The steam condensate that the natural pond slag evaporates enters sewage-treatment plant, discharging after processing up to standard; Fixed gas is delivered to incinerator and is incinerated, or after deodorization device purifies qualified discharge.
Step 6: with the garbage leachate that produces in step 1 and the step 2, the anaerobic fermentation tank of sending into after collecting in the step 4 carries out the anaerobic fermentation of biological processing.
Sorting process is selected the appropriate combination of sorting machineries such as magnetic separator, screening machine, winnowing machine, water concentrator, and this technology is a mature technology, is widely used in the municipal refuse branch and chooses.
According to the sorting technique of " People's Republic of China's prevention and control of environmental pollution by solid wastes method " enforcement manual to component of refuse, domestic waste can be divided into organic matter, inorganic matter and Recyclable three classes.Wherein organic matter comprises animal, plant; Inorganic matter comprises dirt, brick and tile and pottery; Recyclable comprises stationery, plastics, rubber, yarn fabric, glass, metal, wooden bamboo and other.
The present invention separately handles the high heating value rubbish in the composting and organic matter, to organic matter with ooze drop liquid and carry out a biological disposal upon earlier, again will dewatered back merges with high heating value rubbish and carries out burning disposal.Biological and the burning disposal integrated technique of dewatered city domestic garbage can reach desirable treatment effect to domestic waste, can follow minimizing, resource and innoxious treatment principle, can also promote the efficient and the benefit of garbage disposal.
Biological and the burning disposal integrated technique of dewatered city domestic garbage of the present invention, compared with prior art, its advantage is:
(1) to the drying dehydration process of natural pond slag, replace the single-stage or the multi-stage mechanical dewatering process of conventional anaerobic ferment process historic, breakthroughly, saved the flocculating agent and the defoamer of a large amount of costlinesses.
(2) to the drying dehydration process of natural pond slag, sewage disposal can be difficult to biodegradable COD and stay in the dry thing, the small organic molecule that evaporates on a small quantity in the slag steam condensate of natural pond is easy to through conventional sewage treatment process qualified discharge.
(3), the drying and dehydrating of natural pond slag there has been the thermal source guarantee because integrated anaerobic fermentation and burning process.
(4) owing to combine burning process, to the natural pond slag after the organic anaerobic fermentation of biological processing, after the drying processed, send into incinerator and burn, solved the problem of outlet of natural pond slag, and can this point determine exactly rubbish biological treatment plant normally move vital deciding factor.
(5) owing to combine burning process, dried natural pond slag is sent into incinerator and is burned, and makes the organic matter that enters anaerobic fermentation tank need not careful sorting, allows to contain more impurity, makes sorting process to simplify greatly.
(6), ooze drop liquid and send into anaerobic fermentation tank and carry out anaerobic fermentation of biological and handle owing to combine biological treatment.
(7) carry out burning disposal to burning with Recyclable, because this part refuse thermal value is very high, incinerator no longer relies on auxiliary fuel, and this has reduced energy pressure to lacking the imported city of energy of the few oil of coal.
(8) rubbish that part is sorted out reclaims, and has improved the resource level of garbage disposal.
(9) the waste incineration factory of the present invention to having built, sorting and biological treatment factory before can nearby building in addition reach enforcement purpose of the present invention.
(10) the rubbish biological processing plant of the present invention to having built can nearby build in addition and burn factory, reaches enforcement purpose of the present invention.
(11) the present invention no longer relies on auxiliary fuel, and secondary pollution is few, and the utilization efficiency of heat energy height meets current regenerative resource policy, meets circular economy concept.
The specific embodiment
Below specify the present invention by three embodiment.
Embodiment one:
After 1000 tons/day of primary domestic wastes are carried out broken bag, send into separation system, rubbish need be divided into organic matter, inorganic matter, burning with Recyclable and recovery Recyclable by handling by sorting mechanical compositions such as magnetic separator, screening machine, winnowing machine, water concentrators.Wherein burn with Recyclable and comprise yarn fabric and wooden bamboo; Organic matter comprises animal, plant.Recovery comprises metal, glass, stationery, plastics, rubber and other with Recyclable, can directly carry out resource reutilization.Inorganic matter comprises dirt, brick and tile and pottery, sanitary landfills after collecting.
Burning is sent into incinerator with Recyclable and is carried out burning disposal.The incinerator fire box temperature is 800 ℃, and gas residence time is 2 seconds.The high-temperature flue gas that incinerator produces after waste heat recovery, qualified discharge after smoke eliminator purifies; Burn the lime-ash sanitary landfills after collecting that produces.
Organic matter is sent into anaerobic fermentation tank and is carried out the anaerobic fermentation of biological processing, and fermentation temperature is controlled at 35 ℃.
The biogas that anaerobic fermentation produces after purified treatment as gas supply; The natural pond slag that fermentation produces, the steam that utilizes incinerator to produce carries out drying, and dried natural pond slag is sent into incinerator and is carried out burning disposal.The water vapour that evaporates in the slag dry run of natural pond is pumped to sewage treatment plant after condensation is collected, fixed gas is qualified discharge after deodorization device purifies.
The garbage leachate that each stage of garbage disposal produces is sent into anaerobic fermentation tank and is carried out biological resolution process after collecting.
Embodiment two:
After 500 tons/day of primary domestic wastes are carried out broken bag, send into separation system, rubbish need be divided into organic matter, inorganic matter, burning with Recyclable and recovery Recyclable by handling by sorting mechanical compositions such as magnetic separator, screening machine, winnowing machine, water concentrators.Wherein burn with Recyclable and comprise yarn fabric and wooden bamboo; Organic matter comprises animal, plant.Recovery comprises metal, glass, stationery, plastics, rubber and other with Recyclable, can directly carry out resource reutilization.Inorganic matter comprises dirt, brick and tile and pottery, after collecting as the building materials raw material.
Burning is sent into incinerator with Recyclable and is carried out burning disposal.The incinerator fire box temperature is 950 ℃, and gas residence time is 3 seconds.The high-temperature flue gas that incinerator produces after waste heat recovery, qualified discharge after smoke eliminator purifies; The lime-ash that burn to produce after collecting as the building materials raw material.
Organic matter is sent into anaerobic fermentation tank and is carried out the anaerobic fermentation of biological processing, and fermentation temperature is controlled at 55 ℃.
The biogas that anaerobic fermentation produces can be for the gas electricity generator generating after purified treatment; The natural pond slag that fermentation produces, the steam that utilizes incinerator and gas electricity generator waste heat boiler to produce carries out drying, and dried natural pond slag is sent into incinerator and is carried out burning disposal.The water vapour that evaporates in the slag dry run of natural pond is after condensation is collected, and through discharging after the sewage-treatment plant disposal of establishing is up to standard, fixed gas is delivered to incinerator and incinerated.
The garbage leachate that each stage of garbage disposal produces is sent into anaerobic fermentation tank and is carried out biological resolution process after collecting.
Embodiment three:
After 800 tons/day of primary domestic wastes are carried out broken bag, send into separation system, rubbish need be divided into organic matter, inorganic matter, burning with Recyclable and recovery Recyclable by handling by sorting mechanical compositions such as magnetic separator, screening machine, winnowing machine, water concentrators.Wherein burn with Recyclable and comprise yarn fabric and wooden bamboo; Organic matter comprises animal, plant.Recovery comprises metal, glass, stationery, plastics, rubber and other with Recyclable, can directly carry out resource reutilization.Inorganic matter comprises dirt, brick and tile and pottery, sanitary landfills after collecting.
Burning is sent into incinerator with Recyclable and is carried out burning disposal.The incinerator fire box temperature is 850 ℃, and gas residence time is 4 seconds.The high-temperature flue gas that incinerator produces after waste heat recovery, qualified discharge after smoke eliminator purifies; Burn the lime-ash sanitary landfills after collecting that produces.
Organic matter is sent into anaerobic fermentation tank and is carried out the anaerobic fermentation of biological processing, and fermentation temperature is controlled at 40 ℃.
The biogas that anaerobic fermentation produces after purified treatment as gas supply; The natural pond slag that fermentation produces, the steam that utilizes incinerator to produce carries out drying, and dried natural pond slag is sent into incinerator and is carried out burning disposal.The water vapour that evaporates in the slag dry run of natural pond is after condensation is collected, and through discharging after the sewage-treatment plant disposal of establishing is up to standard, fixed gas is delivered to incinerator and incinerated.
The garbage leachate that each stage of garbage disposal produces is sent into anaerobic fermentation tank and is carried out biological resolution process after collecting.
Only be preferred embodiment of the present invention below, but scope of the invention process is not limited.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100518641A CN100560235C (en) | 2006-06-09 | 2006-06-09 | Biogas residue drying and dehydration type municipal solid waste biological and incineration integrated process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100518641A CN100560235C (en) | 2006-06-09 | 2006-06-09 | Biogas residue drying and dehydration type municipal solid waste biological and incineration integrated process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1857802A CN1857802A (en) | 2006-11-08 |
| CN100560235C true CN100560235C (en) | 2009-11-18 |
Family
ID=37296787
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100518641A Expired - Fee Related CN100560235C (en) | 2006-06-09 | 2006-06-09 | Biogas residue drying and dehydration type municipal solid waste biological and incineration integrated process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100560235C (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102374543A (en) * | 2011-08-08 | 2012-03-14 | 南京大学 | Anaerobic fermentation-incineration combined treatment method for organic wastes |
| CN102950137B (en) * | 2011-08-19 | 2015-07-08 | 光大环保科技发展（北京）有限公司 | Kitchen waste collaborative processing method |
| CN104654312B (en) * | 2015-02-27 | 2017-03-01 | 四川欣源绿环保科技有限公司 | A kind of nonflame burning process of solid waste |
| CN104817357B (en) | 2015-04-30 | 2017-10-13 | 湖南屎壳郎环境科技有限公司 | A kind of large organic waste pollutant source comprehensive treatment system in rural area and method |
| CN108421811B (en) * | 2018-03-22 | 2022-03-22 | 成都华凡科技有限公司 | Ecological utilization method for classified collection of domestic waste and planting and breeding waste |
| CN111112282A (en) * | 2019-12-13 | 2020-05-08 | 上海巴安水务股份有限公司 | Improved biochemical treatment method for kitchen waste |
| CN112146100A (en) * | 2020-09-04 | 2020-12-29 | 钟德仁 | Domestic garbage incineration pretreatment method |
| CN112856427A (en) * | 2020-12-21 | 2021-05-28 | 常熟浦发第二热电能源有限公司 | Wet garbage fermentation gas pretreatment method |
| CN116944194A (en) * | 2023-09-21 | 2023-10-27 | 北京扔了么网络科技有限公司 | Garbage recycling treatment method |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4857458A (en) * | 1985-12-05 | 1989-08-15 | Propiorga | Installation and plant for the recovery of energy from waste and residues |
-
2006
- 2006-06-09 CN CNB2006100518641A patent/CN100560235C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4857458A (en) * | 1985-12-05 | 1989-08-15 | Propiorga | Installation and plant for the recovery of energy from waste and residues |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1857802A (en) | 2006-11-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2741936C1 (en) | Method and device for co-combustion of wastes and semi-dry waste sludge | |
| CN100560235C (en) | Biogas residue drying and dehydration type municipal solid waste biological and incineration integrated process | |
| CN201795494U (en) | Refuse pyrolysis produced gas treatment device | |
| CN110976472B (en) | Kitchen waste and household waste co-processing method | |
| CN101758059B (en) | High-pressure pyrolysis treatment method and system for garbage and sludge and application thereof | |
| CN101530856B (en) | Domestic waste incineration process based on mechanical biological joint pretreatment and system thereof | |
| CN201704175U (en) | Sludge processing device | |
| CN102322642A (en) | Sludge drying and incinerating system on basis of incineration of waste grate furnace and treatment method thereof | |
| CN103756697B (en) | Method and system for processing waste and sludge | |
| CN201500671U (en) | Domestic waste incineration system based on combined mechanical and biological pretreatment | |
| CN101786094A (en) | Combined treatment process for household garbage and sewage | |
| CN111023114A (en) | Method for cooperatively treating municipal sludge and kitchen waste | |
| CN105032884A (en) | System and method of synergistic treatment of household garbage and energy resource comprehensive utilization with rotary cement kiln | |
| CN103244957A (en) | Integral treatment method for drying and incinerating sludge | |
| CN100571912C (en) | Biological and the gasification process integrated technique of dewatered city domestic garbage | |
| CN111960632A (en) | Sludge deep dehydration coupling biomass pyrolysis system and method thereof | |
| CN1181935C (en) | Disposal method of municipal solid waste and waste water as resources | |
| CN113182313A (en) | Multi-source organic solid waste disposal system and method for recycling pollutants | |
| CN207514918U (en) | A kind of rubbish cooperates with incinerating and treating device with semi-dry sludge | |
| CN1296150C (en) | Process for treating urban house refuse using dry method cement production system | |
| CN202688162U (en) | Mixed burning and incinerating comprehensive treatment device for anaerobic sludge generated in process of treating domestic garbage leachate | |
| KR20150049087A (en) | Methods and system to energize that containing organic waste, domestic waste | |
| CN212029513U (en) | Kitchen garbage and sludge combined disposal system | |
| CN1857805A (en) | Garbage treating and utilizing process for small town | |
| CN1952089A (en) | Process for preparing fuel derived from urban domestic garbage |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: NANJING LVZHAN ENERGY CO., LTD. Free format text: FORMER OWNER: ZHANG ZHIXIAO Effective date: 20100831 |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 310013 ROOM 402, UNIT 2, BUILDING 59, GUDANG NEW VILLAGE (WEST), XIHU DISTRICT, HANGZHOU CITY, ZHEJIANG PROVINCE TO: 210037 8/F, BUILDING 6, TIANZHENG INTERNATIONAL PLAZA, NO.399, ZHONGYANG ROAD, GULOU DISTRICT, NANJING CITY, JIANGSU PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20100831 Address after: 210037, Nanjing, Jiangsu province Gulou District 399 Central Road No. 6 International Plaza, 8 floor Patentee after: Nanjing Lvzhan Energy Co.,Ltd. Address before: 310013, room 2, building 59, 402 old swing Village (West), Hangzhou, Zhejiang, Xihu District Patentee before: Zhang Zhixiao |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20091118 Termination date: 20130609 |