CN103112841B - A kind of clean energy-saving manufactures technique and the system of carbon product - Google Patents
A kind of clean energy-saving manufactures technique and the system of carbon product Download PDFInfo
- Publication number
- CN103112841B CN103112841B CN201310057241.5A CN201310057241A CN103112841B CN 103112841 B CN103112841 B CN 103112841B CN 201310057241 A CN201310057241 A CN 201310057241A CN 103112841 B CN103112841 B CN 103112841B
- Authority
- CN
- China
- Prior art keywords
- converter
- charing
- activation
- discharge port
- feed
- 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
Abstract
The present invention relates to a kind of production technique and system of carbon product of clean energy-saving.The system that a kind of clean energy-saving of the present invention manufactures carbon product comprises the following steps: contenting carbon material powder-making machine to make powdered carbon; After powdered carbon and tackiness agent mix and blend, send into granulator granulation, granulating and forming temperature is 0 ~ 40 DEG C, and forming pressure is 100 ~ 300kg/cm
2; After the particle drying device produced by tablets press is dried, send into charing converter and carbonize, wherein bake out temperature is 30 ~ 80 DEG C, and drying time is 3 ~ 24 hours, and carbonization temperature is 300 ~ 800 DEG C, and carbonization time is 40 minutes ~ 4 hours; Carbonized material heat material after charing is directly sent into activation converter and carries out activation treatment, wherein activation temperature is 600 ~ 1200 DEG C, and soak time is 4 ~ 24 hours; Activated material is sent into all mixed cooling preparer and be cooled to 40 ~ 80 DEG C, and carry out modulation treatment.
Description
Technical field
The present invention relates to a kind of manufacturing process of carbon product, particularly relate to a kind of production technique and system of carbon product of clean energy-saving.
Background technology
At present, the situation of the energy-saving and emission-reduction of China is very severe, particularly highly energy-consuming, high pollution industry increase too fast, account for the electric power of national industrial energy consumption and sulfur dioxide emissions nearly 70%, iron and steel, coloured, the large industry growth by 20.6% of building materials, refining of petroleum, chemical industry etc. six, therefore, energy-saving and emission-reduction be China's present stage must faced by problem, and the ubiquitous environmental pollution of the production equipment of existing carbon product is serious, the shortcoming of energy utilization rate.
Summary of the invention
The technical problem to be solved in the present invention is to provide the technique that a kind of clean energy-saving manufactures carbon product, and efficiency is high, environmental pollution is little.
A kind of clean energy-saving of the present invention manufactures the technique of carbon product, it is characterized in that, comprises the following steps:
1), contenting carbon material powder-making machine is made powdered carbon;
2), by after powdered carbon and tackiness agent mix and blend, send into granulator granulation, granulating and forming temperature is 0 ~ 40 DEG C, and forming pressure is 100 ~ 300kg/cm
2;
3), after the particle drying device, by tablets press produced is dried, send into charing converter and carbonize, wherein bake out temperature is 30 ~ 80 DEG C, and drying time is 3 ~ 24 hours, and carbonization temperature is 300 ~ 800 DEG C, and carbonization time is 40 minutes ~ 4 hours;
4), by the carbonized material heat material direct feeding activation converter after charing carry out activation treatment, wherein activation temperature is 600 ~ 1200 DEG C, and soak time is 4 ~ 24 hours;
5), by activated material send into all mixed cooling preparer and be cooled to 40 ~ 80 DEG C, and carry out modulation treatment;
6), screening packaging is carried out to the charcoal crude granule screening plant obtained after cooling modulation;
Wherein said tablets press, charing converter, activation converter, screening plant is provided with cleaning apparatus, described tablets press, charing converter, the gas that activation converter and screening plant produce after dedusting is all sent in tail gas burning furnace and is burned, the combustion tail gas that described activation converter and charing converter produce passes into tail gas burning furnace burning, described tail gas burning furnace is connected with waste heat boiler, the steam supply activation converter that waste heat boiler produces and charing converter use, the particle that flue gas after described waste heat boiler uses is produced for drying tablets press by sending into drying unit after smoke eliminator purification.
A kind of clean energy-saving of the present invention manufactures the technique of carbon product, the contenting carbon material that wherein step 1) uses is hard coal, bituminous coal, upgraded brown coal, blue charcoal, charing plant, described hard coal, bituminous coal, upgraded brown coal, blue charcoal, charing plant fugitive constituent be all less than 30%.
A kind of clean energy-saving of the present invention manufactures the technique of carbon product, the mixture that the contenting carbon material that wherein step 1) uses mixes for 70:30 according to weight percent with coke powder for blue charcoal; Or the mixture that the contenting carbon material that step 1) uses is bituminous coal, blue charcoal mixes for 50:30:20 according to weight percent with coke powder; Or the mixture that the contenting carbon material that step 1) uses mixes for 60:40 according to weight percent with coke powder for charing wood chip; Wherein the fugitive constituent of said mixture is all less than 30%.
A kind of clean energy-saving of the present invention manufactures the technique of carbon product, and the contenting carbon material that wherein step 1) uses is the raw material of following parts by weight:
Coke powder or charing powder: 55 ~ 65;
Coking coal or 1/3 coking coal: 15 ~ 35;
Hard coal or bituminous coal: 5 ~ 20.
A kind of clean energy-saving of the present invention manufactures the technique of carbon product, wherein step 2) described in tackiness agent be tar; Or be resin; Or for tar is the mixture that 80:20 mixes with pitch according to weight percent; Or for starch is the mixture that 90:10 mixes with pitch according to weight percent; Or for resin is the mixture that 90:10 mixes with pitch according to weight percent.
A kind of clean energy-saving of the present invention manufactures the technique of carbon product, and the modulation treatment of wherein said step 5) is for adding 0.05 ~ 5%(weight percent) sodium hydroxide or potassium hydroxide or ammoniacal liquor or urea.
The system difference from prior art that a kind of clean energy-saving of the present invention manufactures carbon product is that the present invention passes through by material by drying sticky, more dry by being sticked with, and is cooled again, improve the performance of carbon product by cold heating, after directly entering activation converter activation by making carbonized material heat material, improve the productive rate of activated material, improve quality product, then activation converter heat material is all mixed cooling, make use of the waste heat of material, saved the energy, medicament is sprayed in all mixed cooling preparer, while cooling material, supplement activation, improve the performance of carbon product, by by tablets press, the waste gas that charing converter and screening plant produce after dedusting is all sent in tail gas burning furnace and is burned, the combustion tail gas that activation converter and charing converter produce passes into tail gas burning furnace burning, waste gas and tail gas are thoroughly burnt, and the gas after burning is purified by gas cleaning device, flue gas after simultaneously utilizing purification heats to drying unit, for material drying, the high-temperature steam supply charing converter that waste heat boiler produces and activation converter use, not only avoid tail gas pollution environment, but also improve energy utilization rate, therefore this technique efficiency is high, environmental pollution is little.
Another technical problem that the present invention will solve is to provide the system that a kind of clean energy-saving manufactures carbon product, and this system architecture is compact, efficiency is high, environmental pollution is little.
A kind of clean energy-saving of the present invention manufactures the system of carbon product, comprise powder-making machine, mixing agitator, tablets press, drying unit, charing converter, activation converter, tail gas burning furnace, waste heat boiler, smoke eliminator, all mixed cooling preparer and screening plant, powder-making machine discharge port is connected with the opening for feed of mixing agitator, the opening for feed of mixing agitator is also connected with tackiness agent blend tank, the discharge port of mixing agitator is connected with the opening for feed of tablets press, the discharge port of tablets press is connected with the opening for feed of drying unit, the discharge port of drying unit is connected with the opening for feed of charing converter, the discharge port of charing converter is connected with the opening for feed of activation converter, the discharge port of activation converter is connected with all mixed opening for feed cooling preparer, all mixed cooling preparer is connected with screening plant, charing converter is connected with the inlet mouth of tail gas burning furnace with the activation offgas outlet of converter, the hot-blast outlet of tail gas burning furnace is connected with waste heat boiler, the air outlet of waste heat boiler is connected with the inlet mouth of smoke eliminator, the air outlet of smoke eliminator is communicated with the hot wind inlet of drying unit, the air outlet of drying unit is communicated with air, the vapour outlet that waste heat boiler produces is connected with the steam-in carbonizing converter with activation converter respectively, tablets press, charing converter, screening plant is provided with cleaning apparatus, tablets press, charing converter is all connected with the inlet mouth of tail gas burning furnace with the air outlet of the cleaning apparatus of screening plant, tablets press is positioned at the below of mixing agitator, drying unit is positioned at the below of tablets press, charing converter is positioned at the below of drying unit, activation converter is positioned at the below of charing converter, all mixed cooling preparer is positioned at the below of charing converter, screening plant is positioned at the below of all mixed cooling preparer.
A kind of clean energy-saving of the present invention manufactures the system of carbon product, wherein also comprise powdered carbon storage tank, material-compound tank and tackiness agent tank, the discharge port of powder-making machine is communicated with the opening for feed of powdered carbon storage tank, the discharge port of powdered carbon storage tank is communicated with the opening for feed of mixing agitator by powdered carbon test tank, material-compound tank is connected with the discharge port tackiness agent blend tank of tackiness agent tank, and the discharge port of tackiness agent blend tank is communicated with the opening for feed of mixing agitator by tackiness agent test tank.
A kind of clean energy-saving of the present invention manufactures the system of carbon product; the discharge port of wherein said mixing agitator is connected with the opening for feed of tablets press by screw feeder; the discharge port of tablets press is connected with the opening for feed of drying unit by the first rotary conveyor, and the discharge port of drying unit is connected by the opening for feed of the second rotary conveyor with charing converter.
The system difference from prior art that a kind of clean energy-saving of the present invention manufactures carbon product is that the present invention passes through tablets press, the waste gas that charing converter and screening plant produce after dedusting is all sent in tail gas burning furnace and is burned, the combustion tail gas that activation converter and charing converter produce passes into tail gas burning furnace burning, waste gas and tail gas are thoroughly burnt, and the gas after burning is purified by gas cleaning device, flue gas after simultaneously utilizing purification heats to drying unit, for material drying, the high-temperature steam supply charing converter that waste heat boiler produces and activation converter use, not only avoid tail gas pollution environment, but also improve energy utilization rate, and native system compact construction, the trend of material from high to low, trend rationally, system stability is reliable.
Below in conjunction with accompanying drawing, the system and method that a kind of clean energy-saving of the present invention manufactures carbon product is described further.
Accompanying drawing explanation
Fig. 1 is the structural representation that a kind of clean energy-saving of the present invention manufactures the system of carbon product.
Embodiment
As shown in Figure 1, the system of a kind of clean energy-saving of the present invention manufacture carbon product comprises powder-making machine 1, powdered carbon storage tank 14, material-compound tank 15, tackiness agent tank 16, mixing agitator 2, tablets press 3, drying unit 4, charing converter 5, activation converter 6, tail gas burning furnace 7, waste heat boiler 8, smoke eliminator 9, all mixed cooling preparer 10 and screening plant 11.
The discharge port of powder-making machine 1 is communicated with by the opening for feed of lift with powdered carbon storage tank 14, the discharge port of powdered carbon storage tank 14 is communicated with the opening for feed of mixing agitator 2 by powdered carbon test tank 17, material-compound tank 15 is connected with the discharge port tackiness agent blend tank 12 of tackiness agent tank 16, and the discharge port of tackiness agent blend tank 12 is communicated with the opening for feed of mixing agitator 2 by tackiness agent test tank 18.Tablets press 3 is positioned at the below of mixing agitator 2, and the discharge port of mixing agitator 2 is connected with the opening for feed of tablets press 3 by screw feeder 19.Drying unit 4 is positioned at the below of tablets press 3; the discharge port of tablets press 3 is connected with the opening for feed of drying unit 4 by the first rotary conveyor 20; drying unit can adopt electric dryer or air flow dryer; the present invention uses air flow dryer, utilizes the hot blast after smoke eliminator 9 desulphurization and denitration, dedusting to come for air flow dryer material drying.Charing converter 5 is positioned at the below of drying unit 4, and the discharge port of drying unit 4 is connected by the opening for feed of the second rotary conveyor 21 with charing converter 5.Activation converter 6 is positioned at the below of charing converter 5, the discharge port of charing converter 5 is connected with the opening for feed of activation converter 6, can by the directly supply activation converter 6 of carbonized material heat material, the temperature of the carbonized material heat material of supply is about 40 DEG C, both carbonized material can have been avoided to be oxidized catch fire, can enhance product performance again, reduce operation steps, save energy and cost.All mixed cooling preparer 10 is positioned at the below of charing converter 5, and the discharge port of activation converter 6 is connected with all mixed opening for feed cooling preparer 10, and mixed cooling preparer 10 adopts spray water to cool material, and is provided with dosing mouth, carrys out brewed product for sodium hydroxide etc.Screening plant 11 is positioned at the below of all mixed cooling preparer 10, and all mixed cooling preparer 10 is connected with screening plant 11.Charing converter 5 is connected with the inlet mouth of tail gas burning furnace 7 with the offgas outlet of activation converter 6, the hot-blast outlet of tail gas burning furnace 7 is connected with waste heat boiler 8, the air outlet of waste heat boiler 8 is connected with the inlet mouth of smoke eliminator 9, the air outlet of smoke eliminator 9 is communicated with the hot wind inlet of drying unit 4, the air outlet of drying unit 4 is communicated with air, the vapour outlet that waste heat boiler 8 produces is connected with the steam-in carbonizing converter 5 with activation converter 6 respectively, tablets press 3, charing converter 5, screening plant 11 is provided with cleaning apparatus 13, tablets press 3, charing converter 5 is all connected with the inlet mouth of tail gas burning furnace 7 with the air outlet of the cleaning apparatus 13 of screening plant 11.The pipeline connecting each air inlet/outlet in the present invention is provided with induced draft fan.
In order to make this system reach material again high to Low, trend reasonably arrange; can by this system layout in four layers of buildings; powder-making machine 1, smoke eliminator 9, all mixed cooling preparer 10 and screening plant 11 are arranged in the first layer; activation converter 6, tail gas burning furnace 7 and waste heat boiler 8 are arranged in the second layer; charing converter 5 is arranged in third layer, powdered carbon storage tank 14, material-compound tank 15, tackiness agent tank 16, mixing agitator 2, tablets press 3 and drying unit 4 are arranged in the 4th layer.
Embodiment 1:
All be less than by fugitive constituent after powdered carbon made by the hard coal of 30%, bituminous coal, upgraded brown coal, blue charcoal or charing plant (as wood chip, stalk etc.) feeding powder-making machine and send into powdered carbon storage tank, wherein the granularity of powdered carbon is preferably by 200 eye mesh screens, tar or resin are put into tackiness agent blend tank and is deployed into tackiness agent, after powdered carbon and tackiness agent are sent into mixing agitator mix and blend, send into granulator granulation by screw feeder, granulating and forming temperature is 0 ~ 40 DEG C, and forming pressure is 100 ~ 300kg/cm
2wherein the mold temperature of granulation and pressure can select endpoint value and the intermediate value of two scopes above according to the globule size of granulation and the different operating mode such as raw material, finished product requirement, as granulating and forming temperature can select 0 DEG C or 25 DEG C or 40 DEG C, forming pressure can select 100kg/cm
2or 180kg/cm
2or 300kg/cm
2, after the particle drying device produced by tablets press is dried, send into charing converter to carbonize, wherein bake out temperature is 30 ~ 80 DEG C, drying time is 3 ~ 24 hours, carbonization temperature is 300 ~ 800 DEG C, carbonization time is 40 minutes ~ 4 hours, wherein bake out temperature and time are according to the size of particle and raw material, the different operating modes such as finished product requirement can select endpoint value and the intermediate value of scope above, as bake out temperature can select 30 DEG C or 60 DEG C or 80 DEG C, drying time can select 3 hours or 10 hours or 24 hours, carbonization time and carbonization temperature equally also make the endpoint value at the two ends of scope above and intermediate value can be selected to select according to different operating modes, carbonization temperature can select 300 DEG C or 500 DEG C or 800 DEG C, carbonization time can select 40 minutes or 2 hours or 4 hours, carbonized material heat material after charing is directly sent into activation converter and carries out activation treatment, wherein activation temperature is 600 ~ 1200 DEG C, soak time is 4 ~ 24 hours, activation temperature and soak time can select endpoint value and the intermediate value of scope above according to the size of carbonized material and the different operating mode such as raw material, finished product requirement, as activation temperature can select 600 DEG C or 800 DEG C or 1200 DEG C, soak time can select 4 hours or 15 hours or 24 hours, activated material is sent into all mixed cooling preparer and be cooled to 40 ~ 80 DEG C, as activated material can be cooled to 40 DEG C or 60 DEG C or 80 DEG C, and add weight percent be 0.05% or 3% or 5% sodium hydroxide or potassium hydroxide or ammoniacal liquor or urea carry out modulation treatment, screening packaging is carried out to the charcoal crude granule screening plant obtained after cooling modulation, obtains carbon product.
Embodiment 2:
The present embodiment and the difference of embodiment 1 are only the mixture that the contenting carbon material used when making powdered carbon mixes for 70:30 according to weight percent with coke powder for blue charcoal; Or the mixture that the contenting carbon material used is bituminous coal, blue charcoal mixes for 50:30:20 according to weight percent with coke powder; Or the mixture that the contenting carbon material used mixes for 60:40 according to weight percent with coke powder for charing wood chip; Wherein the fugitive constituent of said mixture is all less than 30%, and the granularity of the powdered carbon that above-mentioned materials is made by powder-making machine is preferably by 200 eye mesh screens.The mixture that the tackiness agent used mixes for 80:20 according to weight percent with pitch for tar; Or for starch is the mixture that 90:10 mixes with pitch according to weight percent; Or for resin is the mixture that 90:10 mixes with pitch according to weight percent.
Embodiment 3:
The difference of the present embodiment and embodiment 1 is only that used powdered carbon is made into powdered carbon by 200 eye mesh screens for coke powder 55 kilograms, 15 kilograms, coking coal and 5 kilograms, hard coal being added powder-making machine; Or the powdered carbon used is made into powdered carbon by 200 eye mesh screens for 60 kilograms, carbonized material powder, 55 kilograms, 1/3 coking coal and 10 kilograms, bituminous coal being added powder-making machine; Or the powdered carbon used is made into powdered carbon by 200 eye mesh screens for coal dust 65 kilograms, 30 kilograms, coking coal and 15 kilograms, hard coal being added powder-making machine; Or the powdered carbon used is made into powdered carbon by 200 eye mesh screens for coke powder 65 kilograms, 30 kilograms, coking coal and 20 kilograms, hard coal being added powder-making machine; Or the powdered carbon used is made into powdered carbon by 200 eye mesh screens for coke powder 65 kilograms, 35 kilograms, coking coal and 20 kilograms, hard coal being added powder-making machine; Or the powdered carbon used is made into powdered carbon by 200 eye mesh screens for coal dust 65 kilograms, 35 kilograms, 1/3 coking coal and 20 kilograms, hard coal being added powder-making machine.
Above-described embodiment is only be described the preferred embodiment of the present invention; not scope of the present invention is limited; under not departing from the present invention and designing the prerequisite of spirit; the various distortion that those of ordinary skill in the art make technical scheme of the present invention and improvement, all should fall in protection domain that claims of the present invention determines.
Claims (8)
1. clean energy-saving manufactures a technique for carbon product, it is characterized in that, comprises the following steps:
1), contenting carbon material powder-making machine is made powdered carbon;
2), by after powdered carbon and tackiness agent mix and blend, send into granulator granulation, granulating and forming temperature is 0 ~ 40 DEG C, and forming pressure is 100 ~ 300kg/cm
2;
3), after the particle drying device, by tablets press produced is dried, send into charing converter and carbonize, wherein bake out temperature is 30 ~ 80 DEG C, and drying time is 3 ~ 24 hours, and carbonization temperature is 300 ~ 800 DEG C, and carbonization time is 40 minutes ~ 4 hours;
4), by the carbonized material heat material direct feeding activation converter after charing carry out activation treatment, wherein activation temperature is 600 ~ 1200 DEG C, and soak time is 4 ~ 24 hours;
5), by activated material send into all mixed cooling preparer and be cooled to 40 ~ 80 DEG C, and carry out modulation treatment, during modulation treatment, add sodium hydroxide or potassium hydroxide or ammoniacal liquor or urea that weight percent is 0.05 ~ 5%;
6), screening packaging is carried out to the charcoal crude granule screening plant obtained after cooling modulation;
Wherein said tablets press, charing converter, screening plant are provided with cleaning apparatus; the gas that described tablets press, charing converter and screening plant produce after dedusting is all sent in tail gas burning furnace and is burned; the combustion tail gas that described activation converter and charing converter produce passes into tail gas burning furnace burning; described tail gas burning furnace is connected with waste heat boiler; the steam supply activation converter that waste heat boiler produces and charing converter use, the particle that the flue gas after described waste heat boiler uses is produced for drying tablets press by sending into drying unit after smoke eliminator purification.
2. a kind of clean energy-saving according to claim 1 manufactures the technique of carbon product, it is characterized in that: wherein step 1) contenting carbon material that uses is hard coal, bituminous coal, upgraded brown coal, blue charcoal, charing plant, the fugitive constituent of described hard coal, bituminous coal, upgraded brown coal, blue charcoal, charing plant is all less than 30%.
3. a kind of clean energy-saving according to claim 1 manufactures the technique of carbon product, it is characterized in that: wherein step 1) mixture that mixes for 70:30 according to weight percent with coke powder for blue charcoal of the contenting carbon material that uses; Or step 1) contenting carbon material that uses is bituminous coal, blue charcoal mixes for 50:30:20 according to weight percent with coke powder mixture; Or step 1) mixture that mixes for 60:40 according to weight percent with coke powder for charing wood chip of the contenting carbon material that uses; Wherein the fugitive constituent of said mixture is all less than 30%.
4. a kind of clean energy-saving according to claim 1 manufactures the technique of carbon product, it is characterized in that: wherein step 1) contenting carbon material that uses is the raw material of following parts by weight:
Coke powder or charing powder: 55 ~ 65;
Coking coal or 1/3 coking coal: 15 ~ 35;
Hard coal or bituminous coal: 5 ~ 20.
5. a kind of clean energy-saving according to Claims 2 or 3 or 4 manufactures the technique of carbon product, it is characterized in that: wherein step 2) described in tackiness agent be tar; Or be resin; Or for tar is the mixture that 80:20 mixes with pitch according to weight percent; Or for starch is the mixture that 90:10 mixes with pitch according to weight percent; Or for resin is the mixture that 90:10 mixes with pitch according to weight percent.
6. the system of a clean energy-saving manufacture carbon product, it is characterized in that: comprise powder-making machine (1), mixing agitator (2), tablets press (3), drying unit (4), charing converter (5), activation converter (6), tail gas burning furnace (7), waste heat boiler (8), smoke eliminator (9), all mixed cooling preparer (10) and screening plant (11), the discharge port of described powder-making machine (1) is connected with the opening for feed of mixing agitator (2), the opening for feed of described mixing agitator (2) is also connected with tackiness agent blend tank (12), the discharge port of described mixing agitator (2) is connected with the opening for feed of tablets press (3), the discharge port of described tablets press (3) is connected with the opening for feed of drying unit (4), the discharge port of described drying unit (4) is connected with the opening for feed of charing converter (5), the discharge port of described charing converter (5) is connected with the opening for feed of activation converter (6), the discharge port of described activation converter (6) is connected with all mixed opening for feed cooling preparer (10), described all mixed cooling preparer (10) is connected with screening plant (11), described charing converter (5) is connected with the inlet mouth of tail gas burning furnace (7) with the offgas outlet of activation converter (6), the hot-blast outlet of described tail gas burning furnace (7) is connected with waste heat boiler (8), the air outlet of described waste heat boiler (8) is connected with the inlet mouth of smoke eliminator (9), the air outlet of described smoke eliminator (9) is communicated with the hot wind inlet of drying unit (4), the air outlet of described drying unit (4) is communicated with air, the vapour outlet that described waste heat boiler (8) produces is connected with activation converter (6) and the steam-in that carbonizes converter (5) respectively, described tablets press (3), charing converter (5), screening plant (11) is provided with cleaning apparatus (13), described tablets press (3), charing converter (5) is all connected with the inlet mouth of tail gas burning furnace (7) with the air outlet of the cleaning apparatus (13) of screening plant (11), described tablets press (3) is positioned at the below of mixing agitator (2), described drying unit (4) is positioned at the below of tablets press (3), described charing converter (5) is positioned at the below of drying unit (4), described activation converter (6) is positioned at the below of charing converter (5), described all mixed cooling preparer (10) is positioned at the below of activation converter (6), described screening plant (11) is positioned at the below of all mixed cooling preparer (10).
7. a kind of clean energy-saving according to claim 6 manufactures the system of carbon product, it is characterized in that: also comprise powdered carbon storage tank (14), material-compound tank (15) and tackiness agent tank (16), the discharge port of described powder-making machine (1) is communicated with the opening for feed of powdered carbon storage tank (14), the discharge port of described powdered carbon storage tank (14) is communicated with the opening for feed of mixing agitator (2) by powdered carbon test tank (17), described material-compound tank (15) is connected with tackiness agent blend tank (12) with the discharge port of tackiness agent tank (16), the discharge port of described tackiness agent blend tank (12) is communicated with the opening for feed of mixing agitator (2) by tackiness agent test tank (18).
8. a kind of clean energy-saving according to claim 7 manufactures the system of carbon product; it is characterized in that: the discharge port of described mixing agitator (2) is connected with the opening for feed of tablets press (3) by screw feeder (19); the discharge port of described tablets press (3) is connected with the opening for feed of drying unit (4) by the first rotary conveyor (20), and the discharge port of described drying unit (4) is connected by the opening for feed of the second rotary conveyor (21) with charing converter (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310057241.5A CN103112841B (en) | 2013-02-22 | 2013-02-22 | A kind of clean energy-saving manufactures technique and the system of carbon product |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310057241.5A CN103112841B (en) | 2013-02-22 | 2013-02-22 | A kind of clean energy-saving manufactures technique and the system of carbon product |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103112841A CN103112841A (en) | 2013-05-22 |
| CN103112841B true CN103112841B (en) | 2015-08-26 |
Family
ID=48411249
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310057241.5A Expired - Fee Related CN103112841B (en) | 2013-02-22 | 2013-02-22 | A kind of clean energy-saving manufactures technique and the system of carbon product |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103112841B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103982900B (en) * | 2014-06-06 | 2017-04-12 | 湖州强马分子筛有限公司 | Environment-friendly and energy-saving combustion treatment method and device |
| CN109264717B (en) * | 2018-12-05 | 2024-01-30 | 诺曼利尔（青岛）环境能源技术有限公司 | Clean production process and system for activated carbon and coke |
| CN115724426A (en) * | 2022-12-06 | 2023-03-03 | 辽宁工程技术大学 | Preparation method of in-situ nitrogen-doped coal-based porous carbon lithium-sulfur battery positive electrode material |
| CN116409787A (en) * | 2023-04-17 | 2023-07-11 | 中国电建集团西北勘测设计研究院有限公司 | Biochar activation forming device and method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101121514A (en) * | 2007-07-27 | 2008-02-13 | 邹炎 | Water purification active carbon prepared from vegetal castoff and preparation method thereof |
| CN101234762A (en) * | 2008-02-27 | 2008-08-06 | 邹炎 | Physical method energy-saving cleaning technique for manufacturing active carbon |
| CN101462721A (en) * | 2009-01-06 | 2009-06-24 | 邹炎 | Technological process for cleaning preparing active carbon and active coke from lignite |
| CN101935031A (en) * | 2010-06-25 | 2011-01-05 | 中国石油天然气集团公司 | Method for separating and recovering carbon from pyrolysis residue of sludge containing oil |
| CN203144112U (en) * | 2013-02-22 | 2013-08-21 | 邹炎 | System for manufacturing carbon products in clean and energy-saving manner |
-
2013
- 2013-02-22 CN CN201310057241.5A patent/CN103112841B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101121514A (en) * | 2007-07-27 | 2008-02-13 | 邹炎 | Water purification active carbon prepared from vegetal castoff and preparation method thereof |
| CN101234762A (en) * | 2008-02-27 | 2008-08-06 | 邹炎 | Physical method energy-saving cleaning technique for manufacturing active carbon |
| CN101462721A (en) * | 2009-01-06 | 2009-06-24 | 邹炎 | Technological process for cleaning preparing active carbon and active coke from lignite |
| CN101935031A (en) * | 2010-06-25 | 2011-01-05 | 中国石油天然气集团公司 | Method for separating and recovering carbon from pyrolysis residue of sludge containing oil |
| CN203144112U (en) * | 2013-02-22 | 2013-08-21 | 邹炎 | System for manufacturing carbon products in clean and energy-saving manner |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103112841A (en) | 2013-05-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101234762B (en) | Physical method energy-saving cleaning technique for manufacturing active carbon | |
| CN101462721B (en) | Technological process for cleaning preparing active carbon and active coke from lignite | |
| CN103112841B (en) | A kind of clean energy-saving manufactures technique and the system of carbon product | |
| CN103922333B (en) | The oxygen carbonization pretreatment system prepared for active carbon from coal | |
| CN103818902B (en) | Multi-stage oven is adopted to manufacture desulphurization denitration activated coke production technique and production unit | |
| CN104164244A (en) | Coal full-grain size grading pyrolysis and active coke preparation coupling process and system in coal gas circulating | |
| CN105752956A (en) | Method and system for preparing phosphoric acid | |
| CN204434292U (en) | Prepare the system of calcium carbide | |
| CN104556037A (en) | Method for preparing calcium carbide | |
| CN209039395U (en) | A kind of stalk is dry and thermal cracker | |
| CN110172539A (en) | Iron content red mud recovery method, rock wool preparation method and corresponding rock wool | |
| CN104211028A (en) | Composite pellet material used for kiln method phosphoric acid technology and molding method thereof | |
| CN102899093B (en) | High-efficiency cleaning coal gasifying process | |
| CN203144112U (en) | System for manufacturing carbon products in clean and energy-saving manner | |
| CN203866039U (en) | Oxidizing and carbonizing pretreatment system for preparing coal-based activated carbon | |
| CN206832029U (en) | The equipment that cement kiln head is burnt using biomass fuel catalysis | |
| CN206858488U (en) | A kind of biomass continuous high-temperature carbonization device | |
| CN102320640A (en) | Method for decomposing phosphogypsum through coupling reaction heat and vibration fluidizing | |
| CN104891490A (en) | Method for producing active carbon in fluidization way | |
| CN204434293U (en) | Prepare the system of calcium carbide | |
| CN210795784U (en) | System for production carbide | |
| CN204039334U (en) | Coal gas circulation coal wholegrain radial sector pyrolysis coupling Active coke preparation system | |
| CN107337208A (en) | A kind of system and method that calcium carbide is produced using biomass pyrolytic | |
| CN107140639A (en) | A kind of focal sphere and its manufacture method | |
| CN202829612U (en) | Novel closed functional type production system of light calcium carbonate |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150826 Termination date: 20200222 |