CN102963890A - Carbonization activation integrated furnace - Google Patents
Carbonization activation integrated furnace Download PDFInfo
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- CN102963890A CN102963890A CN2012103685942A CN201210368594A CN102963890A CN 102963890 A CN102963890 A CN 102963890A CN 2012103685942 A CN2012103685942 A CN 2012103685942A CN 201210368594 A CN201210368594 A CN 201210368594A CN 102963890 A CN102963890 A CN 102963890A
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Abstract
The invention relates to a carbonization activation integrated furnace, which includes a material chamber. The top of the material chamber is provided with a feed inlet, the bottom is provided with a discharge port, and the material chamber is used for storing and transporting materials. A drying section, a carbonization section, and an activation section that are communicated are disposed between the feed inlet and the discharge port from top to bottom in order. The furnace also includes a combustion chamber disposed outside the material chamber and used for heating materials in the material chamber. The activation section of the material chamber is equipped with a steam pipeline, which has several water vapor outlets molded in the vertical direction. The setting mode of the water vapor outlets enables water vapor to contact more materials in the vertical direction, and the water vapor outlets are uniformly distributed and are easy to operate. Meanwhile, water vapor moves in the horizontal direction, thus solving the problem that the pressure of materials above limits the upward movement range of water vapor.
Description
Technical field
The present invention relates to a kind of carbonization-activation integral furnace, specifically a kind of carbonization-activation integral furnace by the outer hot indirect heating of external combustion.
Background technology
The preparation of activated coke or gac need to use the preparation stove to finish, and finishes the process of charing or activation in the preparation stove, finally makes required activated coke or gac.At present, gac/Jiao's preparation stove mainly contains following form, and one is Stepple furnace, mainly uses in China, and it is for being interrupted the mode of production, and the separate unit treatment capacity is low, only has the hundreds of ton every year; Another kind is multiple hearth furnace, is derived from the U.S., and the body of heater shell of multiple hearth furnace is cylindrical, is rolled by general steel plate to form; Inner lining refractory, with heterotypic fire brick or common laying fireproof bricks hearth structure and make stove be partitioned into multistage, every section siege respectively around siege and/or middle section material falling hole is set, solid materials stirs, enters next section siege by the stirrer gear that is installed on the slow speed of revolution central shaft agitating arm step by step by lateral on the siege inboard (on lower floor's siege then by the inboard laterally), this stove design is comparatively complicated, and very high to equipment requirements such as central shaft, rake teeths.In addition, above-mentioned Stepple furnace and multiple hearth furnace can only be finished activation, and charing need to be carried out in independent equipment, has strengthened the complicacy of production technique.Also has a kind of pierce smith converter that is, because its material advances by body of heater self angle of inclination and oblique flight, the rate of advance of the bad control material of production lightweight charcoal, and above-mentioned activation furnace all is interior heating, combustion gases directly contact with material, inevitably cause the raw material surface combustion, reduce the quality of gac, and because the heating unit of pierce smith converter is arranged on the below usually, so need to ceaselessly rotating the guarantee material, material barrel is heated evenly.
In the prior art, Chinese patent literature CN2535399 discloses a kind of bucket-type carbon activation furnace apparatus, comprise furnace wall, storagetank, the oxidation air flue, combustion chamber, cooling zone, the water vapour import, discharger, discharging hopper, blast pipe, dividing plate, the side flue, exhanst gas outlet, packing, the stove seat, crown cap, water seal, combustion chamber in the furnace wall is to be arranged in order with the bucket type brick to form, laterally consist of horizontal air flue between the adjacent brick wall, repeatedly put up and down, consist of vertical material road between the brick hole, joint, brick hole forms venting port, horizontal air flue communicates with the side flue that is provided with blast pipe, dividing plate is divided into arid zones to combustion chamber, carbide bound, activation zone, the bucket type brick is the hollow brick of outer image bucket, the upper surface of brick is square, and brick hole inwall section is trapezoidal, on the brick inwall leg is set.Described bucket type brick is that profile is round table-like hollow brick, and the upper surface of brick is square, and brick hole inwall section is trapezoidal, on the brick inwall leg is set.Described bucket type brick is the hollow brick of outer image bucket, and the upper surface of brick is square, and brick hole inwall section is trapezoidal, and front and back brick wall face is vertical surface, and left and right sides brick wall face is the inclined-plane.The oxidation air flue of oxygenizement has been set on combustion chamber top.The water vapor inlet mouth is arranged on the bottom of cooling zone.Exhanst gas outlet is arranged on bottom of furnace body side flue or is arranged on body of heater top side flue.
The vertical material road that above-described bucket type brick forms, there is opening joint, brick hole, make the volatile matter of the rear material that is heated to precipitate into horizontal air flue, this structure is directly exposed in the smoke chamber partial material, when volatile matter is separated out, partial material can be brought in the smoke chamber, pollute and the waste of raw material, flue gas directly contacts the burning that can cause material with material simultaneously, affects the quality of gac; And the required water vapor as activator of above-mentioned activation zone, its inlet mouth is arranged on the bottom of cooling zone, water vapor need to pass through cooling zone, the reduction temperature of charge becomes superheated vapour and enters material road activation zone after heat exchange, material is activated, because water vapor enters activation zone from the bottom, water vapour moves from the bottom to top, be subject to the inhibition of top pressure and material, the water vapor range ability that makes progress is little, so just limit the scope of activation zone, activation efficiency is reduced, thereby affected the production efficiency of product.Although the activating apparatus of described pierce smith converter is inserted into material barrel inside, but just by activating apparatus top end opening place ejection water vapor, the rotation by material barrel makes water vapor diffusion even, in addition, the body of heater rotation needs to use very large power, and the complex structure of this body of heater.
Summary of the invention
Technical problem to be solved by this invention is that the activator feedway is arranged on the activation section below in the prior art, the water vapor range ability that makes progress is little, range of activation and activation efficiency have been affected, thereby provide a kind of water vapor that can make evenly to distribute at described activation section, thereby improve the carbonization-activation integral furnace of activation efficiency.
For solving the problems of the technologies described above, the present invention is achieved by the following technical solutions:
A kind of carbonization-activation integral furnace comprises:
Supplies room, described supplies room top is provided with opening for feed, and the bottom is provided with discharge opening, is used for storage and convey materials, sets gradually from top to bottom the dryer section of connection between described opening for feed and described discharge opening, charing section, activation section;
The combustion chamber is arranged on the outside of described supplies room, is used for the material in the described supplies room is heated;
At the activation section of described supplies room, vertically be provided with from the bottom to top steam-pipe, described steam-pipe forms several steam outlets at vertical direction.
Described steam outlet evenly arranges.
Described steam outlet is provided with 400-600.
Form production well on the outer wall of described supplies room, described production well evenly distributes and is angling hole, and the vergence direction of described production well is higher than it towards an end of described supplies room for the end towards described combustion chamber.
Be provided with burner on the sidewall of described combustion chamber, described burner layered arrangement, every layer of described burner is arranged on around the described body of heater uniformly, and the described burner of layering setting is arranged on the middle hypomere of described body of heater.
Described sidewall of combustion chamber below is provided with lets out the ash mouth.
Be provided with exhaust gases passes in the described combustion chamber, the top of described combustion chamber is provided with flue gas processing device, and described flue gas processing device comprises fly-ash separator, induced draft fan and the chimney that connects successively.
Described discharge opening lower end is connected with refrigerating unit.
Described refrigerating unit comprises vapour line and circulating water pipework, and described vapour line is connected with described water vapour pipeline.
Described supplies room is at least one.
Technique scheme of the present invention has the following advantages compared to existing technology:
(1) a kind of carbonization-activation integral furnace of the present invention, comprise supplies room, described supplies room top is provided with opening for feed, the bottom is provided with discharge opening, be used for storage and convey materials, between described opening for feed and described discharge opening, set gradually from top to bottom the dryer section of connection, charing section, activation section; The combustion chamber is arranged on the outside of described supplies room, is used for the material in the described supplies room is heated; At the activation section of described supplies room, vertically be provided with from the bottom to top steam-pipe, described steam-pipe forms several steam outlets at vertical direction.The set-up mode of described steam outlet, make the water vapor in the vertical direction touch more material, and be evenly distributed convenient operation, simultaneously water vapor is to horizontal motion, reduced because the pressure of top material causes the water vapor range limited problem that moves up.
(2) form production well on the outer wall of supplies room of the present invention, described production well evenly distributes and is angling hole, and the vergence direction of described production well is higher than it towards an end of described supplies room for the end towards described combustion chamber.Described charing section material is heated the coal gas of rear generation, described activation section material is heated the water-gas of rear generation, enter in the described combustion chamber by this production well, combustion reactions occurs, the high-temperature flue gas that produces can heat material, and the setting of described production well re-uses inflammable gas, both reduce the coal gas treatment process, also avoided calorific loss simultaneously; Secondly, described production well is obliquely installed, and makes coal gas when entering described combustion chamber, is unlikely to described material is together brought into into the combustion chamber, has avoided waste and the pollution of resource.
(3) be provided with burner on the sidewall of combustion chamber of the present invention, described burner layered arrangement, every layer of described burner is arranged on around the described body of heater uniformly, and the described burner of layering setting is arranged on the middle hypomere of described body of heater.Described burner places the below of described combustion chamber, adds thermogenetic hot flue gas from bottom to top by described supplies room outer wall and heat exchange, and temperature reduces gradually, thus the calorific loss of having avoided the discharging high-temperature flue gas to bring.
Description of drawings
For content of the present invention is more likely to be clearly understood, below in conjunction with accompanying drawing, the present invention is further detailed explanation, wherein,
Fig. 1 is the front view of a kind of carbonization-activation integral furnace of the present invention;
Fig. 2 is the vertical view of a kind of carbonization-activation integral furnace of the present invention;
Fig. 3 is the synoptic diagram of the production well of supplies room outer wall of the present invention.
Reference numeral is expressed as among the figure:
The 1-opening for feed, 2-dryer section, 3-charing section, 4-activation section, the 5-steam-pipe, 6-vapour line, 7-discharge valve, 8-refrigerating unit, 9-circulating water pipework, 10-are let out ash mouth, 11-burner, 12-fly-ash separator, the 13-induced draft fan, 14-chimney, 15-water vapour, 16-coal gas, 17-water-gas, 18-discharge opening, 19-supplies room, the 20-flue, 21-combustion chamber, 22-production well.
Embodiment
As Figure 1-3, in the present embodiment, described a kind of carbonization-activation integral furnace, its ecto-entad comprises combustion chamber 21 successively, supplies room 19;
Described supplies room 19 tops are provided with opening for feed 1, and the bottom is provided with discharge opening 18, are used for storage and convey materials, set gradually from top to bottom the dryer section 2 of connection between described opening for feed 1 and described discharge opening 18, charing section 3, activation section 4;
Described combustion chamber 21 is arranged on the outside of described supplies room 19, is used for the material in the described supplies room 19 is heated;
Wherein, at the activation section 4 of described supplies room 19, vertically be provided with from the bottom to top steam-pipe 5, be used for providing activation section 4 the required water vapor as activator, described steam-pipe 5 forms several steam outlets at vertical direction.And described steam outlet evenly arranges, and as preferred embodiment, described steam outlet is provided with 500.As other can conversion embodiment, steam outlet herein also can be selected 400-600.The set-up mode of described steam outlet, make the water vapor in the vertical direction touch more material, and be evenly distributed convenient operation, simultaneously water vapor is to horizontal motion, reduced because the pressure of top material causes the water vapor range limited problem that moves up.
On the basis of above-described embodiment, further the outer wall at described supplies room 19 forms production well 22, described production well 22 evenly distributes and is angling hole, and the vergence direction of described production well 22 is higher than it towards an end of described supplies room 19 for the end towards described combustion chamber 21.Described dryer section 2 materials are heated the water vapor 15 of rear generation, described charing section 3 materials are heated the coal gas 16 of rear generation, described activation section 4 materials are heated the water-gas 17 of rear generation, enter in the described combustion chamber 21 by this production well 22, combustion reactions occurs, the high-temperature flue gas of generation can heat material, the setting of described production well 22, inflammable gas is re-used, both reduced the coal gas treatment process, also avoided calorific loss simultaneously; Secondly, described production well 22 is obliquely installed, and makes coal gas when entering described combustion chamber 21, is unlikely to material is together brought into into described combustion chamber 21, has avoided waste and the pollution of resource.
Be provided with burner 11 on the sidewall of described combustion chamber 21, described burner 11 layered arrangement, every layer of described burner 11 is arranged on around the described body of heater uniformly, and the described burner 11 of layering setting is arranged on the middle hypomere of described body of heater.Described burner 11 places the below of described combustion chamber 21, adds thermogenetic hot flue gas from bottom to top by described supplies room 19 outer walls and heat exchange, and temperature reduces gradually, thus the calorific loss of having avoided the discharging high-temperature flue gas to bring.
As preferred embodiment, 21 sidewalls below in described combustion chamber is provided with lets out ash mouth 10.
Be provided with exhaust gases passes 20 in the described combustion chamber 21, the tortuous flue that described exhaust gases passes 20 is made of temperature-resistant material, hot flue gas is by the outer wall homogeneous heating of tortuous flue with described supplies room 19.
As preferably, described supplies room 19 can be set to a plurality of, when arranging when a plurality of, between the outer wall of described supplies room 19 certain distance is arranged, and described distance can make flue gas pass through, and guarantees that the outer wall-heated of each described supplies room 19 is even.
The top of described combustion chamber 21 is provided with flue gas processing device, and described flue gas processing device comprises fly-ash separator 12, induced draft fan 13 and the chimney 14 that connects successively.
Described discharge opening 18 lower ends are provided with discharge valve 7, and the time of the carbonization-activation by described discharge valve 7 adjustable materials, when opening described discharge valve 7, the cold slag machine that described activation material enters into the described refrigerating unit 8 of below cools off.
Described refrigerating unit 8 comprises vapour line 6 and circulating water pipework 9, and described vapour line 6 is connected with described steam-pipe 5.The water vapor of absorbing heat enters into described steam-pipe 5 by described vapour line 6, and the material of described activation section 4 is activated.Certainly, as selectable embodiment, described activation section 4 described water vapors also can be supplied with water vapor to described water vapor pipeline 5 by other devices, and selected embodiment can farthest utilize the heat of native system self in the present embodiment, improves thermo-efficiency.
Described refrigerating unit 8 can according to the setting supporting with it of the number of described supplies room 19, also can be connected described discharge opening 18 places of a plurality of described supplies rooms 19 with same described refrigerating unit 8.
Obviously, above-described embodiment only is for example clearly is described, and is not the restriction to embodiment.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here need not also can't give all embodiments exhaustive.And the apparent variation of being extended out thus or change still are among protection scope of the present invention.
Claims (10)
1. carbonization-activation integral furnace comprises:
Supplies room (19), described supplies room (19) top is provided with opening for feed (1), the bottom is provided with discharge opening (18), be used for storage and convey materials, between described opening for feed (1) and described discharge opening (18), set gradually from top to bottom the dryer section (2) of connection, charing section (3), activation section (4);
Combustion chamber (21) is arranged on the outside of described supplies room (19), is used for the material in the described supplies room (19) is heated;
It is characterized in that the activation section (4) in described supplies room (19) vertically is provided with steam-pipe (5) from the bottom to top, described steam-pipe (5) forms several steam outlets at vertical direction.
2. a kind of carbonization-activation integral furnace according to claim 1 is characterized in that, described steam outlet evenly arranges.
3. a kind of carbonization-activation integral furnace according to claim 1 and 2 is characterized in that, described steam outlet is provided with 400-600.
4. arbitrary described a kind of carbonization-activation integral furnace according to claim 1-3, it is characterized in that, form production well (22) on the outer wall of described supplies room (19), described production well (22) evenly distributes and is angling hole, and the vergence direction of described production well (22) is higher than it towards an end of described supplies room (19) for the end towards described combustion chamber (21).
5. arbitrary described a kind of carbonization-activation integral furnace according to claim 1-4, it is characterized in that, be provided with burner (11) on the sidewall of described combustion chamber (21), described burner (11) layered arrangement, every layer of described burner (11) is arranged on around the described body of heater uniformly, and the described burner (11) of layering setting is arranged on the middle hypomere of described body of heater.
6. arbitrary described a kind of carbonization-activation integral furnace is characterized in that according to claim 1-5, and sidewall below in described combustion chamber (21) is provided with lets out ash mouthful (10).
7. arbitrary described a kind of carbonization-activation integral furnace according to claim 1-6, it is characterized in that, be provided with exhaust gases passes (20) in the described combustion chamber (21), the top of described combustion chamber (21) is provided with flue gas processing device, and described flue gas processing device comprises fly-ash separator (12), induced draft fan (13) and the chimney (14) that connects successively.
8. arbitrary described a kind of carbonization-activation integral furnace is characterized in that according to claim 1-7, and described discharge opening (18) lower end is connected with refrigerating unit (8).
9. arbitrary described a kind of carbonization-activation integral furnace is characterized in that according to claim 1-8, and described refrigerating unit (8) comprises vapour line (6) and circulating water pipework (9), and described vapour line (6) is connected with described steam-pipe (5).
10. arbitrary described a kind of carbonization-activation integral furnace is characterized in that according to claim 1-9, and described supplies room (19) is at least one.
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Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103395782A (en) * | 2013-08-08 | 2013-11-20 | 北京金润华扬科技有限公司 | Movable carbon activation method |
| CN103449432A (en) * | 2013-08-30 | 2013-12-18 | 林旭 | Spouted type activation furnace and method for producing super-capacitor carbon by virtue of same |
| CN104100980A (en) * | 2014-07-01 | 2014-10-15 | 同济大学 | Small garbage coking combustion furnace |
| CN104310393A (en) * | 2014-09-29 | 2015-01-28 | 大连理工大学 | Device for continuously preparing activated carbon and method for preparing activated carbon by utilizing device |
| CN107954426A (en) * | 2017-12-08 | 2018-04-24 | 山东汉菱电气有限公司 | For generating the device of activated carbon |
| CN108190852A (en) * | 2017-12-21 | 2018-06-22 | 湖南顶立科技有限公司 | A kind of multistage vertical type continuous carbonization furnace |
| CN109368641A (en) * | 2018-12-12 | 2019-02-22 | 宁夏尼西活性炭有限公司 | A kind of active carbon prepares fuel gas recycling device |
| CN109607536A (en) * | 2019-01-30 | 2019-04-12 | 淮北航浩新材料科技有限公司 | It is a kind of to be carbonized and activate combined vertical furnace |
| CN109629042A (en) * | 2019-02-13 | 2019-04-16 | 江苏苏通碳纤维有限公司 | A kind of carbon activation integral furnace continuously preparing phenolic resin based activated carbon fiber |
| CN110734066A (en) * | 2019-10-24 | 2020-01-31 | 东南大学 | internal and external heating self-heating biomass carbonization-activation device and method |
| CN110819363A (en) * | 2019-10-24 | 2020-02-21 | 东南大学 | Multi-cavity series self-heating external heating converter biomass carbonization-activation device and method |
| CN111807364A (en) * | 2020-08-11 | 2020-10-23 | 聚农(湖州)新能源科技有限公司 | Movable miniaturized biomass continuous steam activation method and activation machine |
| CN113636694A (en) * | 2021-09-07 | 2021-11-12 | 北京国电富通科技发展有限责任公司 | Transformer substation/convertor station domestic sewage treatment system and treatment method |
| CN117146256A (en) * | 2023-08-31 | 2023-12-01 | 青岛冠宝林活性炭有限公司 | Method for co-production of activated carbon and steam and comprehensive utilization of heat energy |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2535399Y (en) * | 2002-03-29 | 2003-02-12 | 林勇胜 | Bucket-type carbon activation furnace apparatus |
| US20110132738A1 (en) * | 2009-12-09 | 2011-06-09 | Barry Louis T | Method and Apparatus for Efficient Production of Activated Carbon |
| CN102295282A (en) * | 2011-08-08 | 2011-12-28 | 北京国电富通科技发展有限责任公司 | Carbonization and activation integral furnace |
| CN202246074U (en) * | 2011-09-19 | 2012-05-30 | 山东科技大学 | Carbonization furnace for activated coke production |
| CN102649550A (en) * | 2011-02-25 | 2012-08-29 | 王全祥 | Carbonization-activation integrated activated carbon production apparatus |
-
2012
- 2012-09-28 CN CN201210368594.2A patent/CN102963890B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2535399Y (en) * | 2002-03-29 | 2003-02-12 | 林勇胜 | Bucket-type carbon activation furnace apparatus |
| US20110132738A1 (en) * | 2009-12-09 | 2011-06-09 | Barry Louis T | Method and Apparatus for Efficient Production of Activated Carbon |
| CN102649550A (en) * | 2011-02-25 | 2012-08-29 | 王全祥 | Carbonization-activation integrated activated carbon production apparatus |
| CN102295282A (en) * | 2011-08-08 | 2011-12-28 | 北京国电富通科技发展有限责任公司 | Carbonization and activation integral furnace |
| CN202246074U (en) * | 2011-09-19 | 2012-05-30 | 山东科技大学 | Carbonization furnace for activated coke production |
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103395782A (en) * | 2013-08-08 | 2013-11-20 | 北京金润华扬科技有限公司 | Movable carbon activation method |
| CN103449432A (en) * | 2013-08-30 | 2013-12-18 | 林旭 | Spouted type activation furnace and method for producing super-capacitor carbon by virtue of same |
| CN103449432B (en) * | 2013-08-30 | 2015-05-06 | 林旭 | Spouted type activation furnace and method for producing super-capacitor carbon by virtue of same |
| CN104100980A (en) * | 2014-07-01 | 2014-10-15 | 同济大学 | Small garbage coking combustion furnace |
| CN104310393A (en) * | 2014-09-29 | 2015-01-28 | 大连理工大学 | Device for continuously preparing activated carbon and method for preparing activated carbon by utilizing device |
| CN104310393B (en) * | 2014-09-29 | 2016-08-17 | 大连理工大学 | The device of a kind of continuous prodution activated carbon and utilize the method that this device prepares activated carbon |
| CN107954426A (en) * | 2017-12-08 | 2018-04-24 | 山东汉菱电气有限公司 | For generating the device of activated carbon |
| CN108190852A (en) * | 2017-12-21 | 2018-06-22 | 湖南顶立科技有限公司 | A kind of multistage vertical type continuous carbonization furnace |
| CN109368641A (en) * | 2018-12-12 | 2019-02-22 | 宁夏尼西活性炭有限公司 | A kind of active carbon prepares fuel gas recycling device |
| CN109368641B (en) * | 2018-12-12 | 2024-02-20 | 宁夏尼西活性炭有限公司 | Device for recycling combustible gas prepared from activated carbon |
| CN109607536B (en) * | 2019-01-30 | 2023-08-08 | 安徽宝隽机车部件有限公司 | Carbonization and activation combined type vertical furnace |
| CN109607536A (en) * | 2019-01-30 | 2019-04-12 | 淮北航浩新材料科技有限公司 | It is a kind of to be carbonized and activate combined vertical furnace |
| CN109629042A (en) * | 2019-02-13 | 2019-04-16 | 江苏苏通碳纤维有限公司 | A kind of carbon activation integral furnace continuously preparing phenolic resin based activated carbon fiber |
| CN110819363B (en) * | 2019-10-24 | 2021-06-01 | 东南大学 | Multi-cavity series self-heating external heating converter biomass carbonization-activation device and method |
| CN110734066B (en) * | 2019-10-24 | 2023-04-21 | 东南大学 | Internal and external heating self-heating type integrated biomass carbonization-activation device and method |
| CN110819363A (en) * | 2019-10-24 | 2020-02-21 | 东南大学 | Multi-cavity series self-heating external heating converter biomass carbonization-activation device and method |
| CN110734066A (en) * | 2019-10-24 | 2020-01-31 | 东南大学 | internal and external heating self-heating biomass carbonization-activation device and method |
| CN111807364A (en) * | 2020-08-11 | 2020-10-23 | 聚农(湖州)新能源科技有限公司 | Movable miniaturized biomass continuous steam activation method and activation machine |
| CN113636694A (en) * | 2021-09-07 | 2021-11-12 | 北京国电富通科技发展有限责任公司 | Transformer substation/convertor station domestic sewage treatment system and treatment method |
| CN117146256A (en) * | 2023-08-31 | 2023-12-01 | 青岛冠宝林活性炭有限公司 | Method for co-production of activated carbon and steam and comprehensive utilization of heat energy |
| CN117146256B (en) * | 2023-08-31 | 2024-04-09 | 青岛冠宝林活性炭有限公司 | Method for co-production of activated carbon and steam and comprehensive utilization of heat energy |
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| CN102963890B (en) | 2015-04-01 |
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