CN203144112U - System for manufacturing carbon products in clean and energy-saving manner - Google Patents
System for manufacturing carbon products in clean and energy-saving manner Download PDFInfo
- Publication number
- CN203144112U CN203144112U CN2013200826991U CN201320082699U CN203144112U CN 203144112 U CN203144112 U CN 203144112U CN 2013200826991 U CN2013200826991 U CN 2013200826991U CN 201320082699 U CN201320082699 U CN 201320082699U CN 203144112 U CN203144112 U CN 203144112U
- Authority
- CN
- China
- Prior art keywords
- converter
- feed
- discharge port
- opening
- drying unit
- 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
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to a system for manufacturing carbon products in a clean and energy-saving manner. The system comprises a flour mill, a mixed stirrer, a pelletizer, a drying device, a carbonizing converter, an activating converter, a tail gas incinerator, a waste heat boiler, a glue gas purifying device, a uniform mixing cooling preparer and a sieving device. The pelletizer is located below the mixed stirrer, the dying device is located below the pelletizer, the carbonizing converter is located below the drying device, the activating converter is located below the carbonizing converter, the uniform mixing cooling prepare is located below the carbonizing converter, and the sieving device is located below the uniform mixing cooling preparer. The system for manufacturing carbon products in the clean and energy-saving manner provided by the utility model is compact in structure, high in energy efficiency and small in environmental pollution.
Description
Technical field
The utility model relates to a kind of manufacturing system of carbon product, particularly relates to a kind of 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 six big industries such as the electric power, iron and steel of national industrial energy consumption and sulfur dioxide emissions nearly 70%, coloured, building materials, refining of petroleum, chemical industry and increase by 20.6%, therefore, energy-saving and emission-reduction are problems that China must face present stage, and the ubiquitous environmental pollution of the production equipment of existing carbon product is serious, the shortcoming of energy utilization rate.
The utility model content
The technical problems to be solved in the utility model provides the system that a kind of clean energy-saving is made carbon product, and this system architecture compactness, efficiency height, environmental pollution are little.
A kind of clean energy-saving of the utility model is made the system of carbon product; comprise powder-making machine; mixing agitator; tablets press; drying unit; the charing converter; the activation converter; tail gas burning furnace; waste heat boiler; smoke eliminator; all mix cooling preparer and screening plant; the powder-making machine discharge port is connected with the opening for feed of mixing agitator; the opening for feed of mixing agitator also is connected with the 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 the opening for feed that all mixes the cooling preparer; all mixing the cooling preparer is connected with screening plant; the tail gas outlet of charing converter and activation converter is connected with the inlet mouth of tail gas burning furnace; 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 blast import of drying unit; the air outlet of drying unit is communicated with atmosphere; the vapour outlet that waste heat boiler produces is connected with the steam-in of activation converter and charing converter respectively; tablets press; the charing converter; be provided with cleaning apparatus on the screening plant; tablets press; the air outlet of the cleaning apparatus of charing converter and screening plant all is connected with the inlet mouth of tail gas burning furnace; tablets press is positioned at the below of mixing agitator; drying unit is positioned at the below of tablets press; the charing converter is positioned at the below of drying unit; the activation converter is positioned at the below of charing converter; all mix and cool off the below that preparer is positioned at the charing converter, screening plant is positioned at the below of all mixing the cooling preparer.
A kind of clean energy-saving of the utility model is made the system of carbon product, wherein also comprise powdered carbon storage tank, material-compound tank and tackiness agent jar, 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 the powdered carbon test tank, the discharge port tackiness agent blend tank of material-compound tank and tackiness agent jar is connected, and the discharge port of tackiness agent blend tank is communicated with the opening for feed of mixing agitator by the tackiness agent test tank.
A kind of clean energy-saving of the utility model is made 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 first rotary conveyor, and the discharge port of drying unit is connected with the opening for feed of charing converter by second rotary conveyor.
System's difference from prior art that a kind of clean energy-saving of the utility model is made carbon product is that the utility model passes through tablets press; the waste gas that charing converter and screening plant produce after dedusting is all sent in the tail gas burning furnace and is burned; the combustion tail gas that activation converter and charing converter produce feeds the tail gas burning furnace burning; waste gas and tail gas are thoroughly burnt; and the gas after will burning purifies by gas cleaning device; utilize flue gas after being purified to heat to drying unit simultaneously; be used for the oven dry material; high-temperature steam supply charing converter and activation converter that waste heat boiler produces are used; not only avoided the tail gas pollution environment; but also improved energy utilization rate; and native system compact construction; the trend of material from high to low; trend is reasonable, and system stability is reliable.
The system that a kind of clean energy-saving of the present utility model is made carbon product below in conjunction with accompanying drawing is described further.
Description of drawings
Fig. 1 is the structural representation that a kind of clean energy-saving of the utility model is made the system of carbon product.
Embodiment
As shown in Figure 1, a kind of clean energy-saving of the utility model system that makes carbon product comprises powder-making machine 1, powdered carbon storage tank 14, material-compound tank 15, tackiness agent jar 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 mixes 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, the discharge port tackiness agent blend tank 12 of material-compound tank 15 and tackiness agent jar 16 is connected, 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 first rotary conveyor 20; drying unit can adopt electric dryer or air flow dryer; the utility model uses air flow dryer, utilizes the hot blast after smoke eliminator 9 desulfurization, denitration, dedusting to come to be air flow dryer oven dry material.Charing converter 5 is positioned at the below of drying unit 4, and the discharge port of drying unit 4 is connected with the opening for feed of charing converter 5 by second rotary conveyor 21.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 be with the directly supply activation converter 6 of carbonized material heat material, the temperature of the carbonized material heat material of supply is about 40 ℃, both can avoid the carbonized material oxidation to catch fire, can enhance product performance again, reduce operation steps, save energy and cost.All mix and cool off the below that preparer 10 is positioned at charing converter 5, activate the discharge port of converter 6 and be connected with the opening for feed that all mixes cooling preparer 10, mix and cool off preparer 10 employing spray waters cooling materials, and be provided with dosing mouth, be used for sodium hydroxide and wait brewed product.Screening plant 11 is positioned at the below of all mixing cooling preparer 10, all mixes cooling preparer 10 and is connected with screening plant 11.The tail gas outlet of charing converter 5 and activation converter 6 is connected with the inlet mouth of tail gas burning furnace 7; 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 blast import of drying unit 4; the air outlet of drying unit 4 is communicated with atmosphere; the vapour outlet that waste heat boiler 8 produces is connected with the steam-in of activation converter 6 and charing converter 5 respectively; tablets press 3; charing converter 5; be provided with cleaning apparatus 13 on the screening plant 11, tablets press 3; the air outlet of the cleaning apparatus 13 of charing converter 5 and screening plant 11 all is connected with the inlet mouth of tail gas burning furnace 7.Be provided with induced draft fan on the pipeline of each air inlet/outlet of connection in the utility model.
In order to make this system reach that material is high again reasonably to be arranged to low, trend; can be with this system layout in four one storey buildings; with powder-making machine 1, smoke eliminator 9, all mix cooling preparer 10 and screening plant 11 and be arranged in the first layer; to activate converter 6, tail gas burning furnace 7 and waste heat boiler 8 and be arranged in the second layer; charing converter 5 is arranged in the 3rd layer, powdered carbon storage tank 14, material-compound tank 15, tackiness agent jar 16, mixing agitator 2, tablets press 3 and drying unit 4 are arranged in the 4th layer.
Embodiment 1:
Fugitive constituent all sent into less than 30% hard coal, bituminous coal, upgrading brown coal, blue charcoal or charing plant (as wood chip, stalk etc.) send into the powdered carbon storage tank after powder-making machine is made powdered carbon, wherein the granularity of powdered carbon is preferably and can passes through 200 eye mesh screens; Tar or resin are put into the tackiness agent blend tank be deployed into tackiness agent; With powdered carbon and tackiness agent send into mixing agitator mix stir after, send into the tablets press granulation by screw feeder, the granulating and forming temperature is 0 ~ 40 ℃, forming pressure is 100 ~ 300kg/cm
2Wherein the mold temperature of granulation and pressure can be selected endpoint value and the intermediate value of top two scopes according to different operating modes such as the globule size of granulation and raw material, finished product requirements, can select 0 ℃ or 25 ℃ or 40 ℃ as the granulating and forming temperature, forming pressure can be selected 100kg/cm
2Perhaps 180kg/cm
2Perhaps 300kg/cm
2After the particle drying device oven dry with tablets press production, send into the charing converter and carry out charing, wherein bake out temperature is 30 ~ 80 ℃, drying time is 3 ~ 24 hours, carbonization temperature is 300 ~ 800 ℃, carbonization time is 40 minutes ~ 4 hours, wherein bake out temperature and time are according to size and the raw material of particle, different operating modes such as finished product requirement can be selected endpoint value and the intermediate value of top scope, can select 30 ℃ or 60 ℃ or 80 ℃ as bake out temperature, drying time can be selected 3 hours or 10 hours or 24 hours, carbonization time equally also makes according to different operating modes with carbonization temperature can select endpoint value and the intermediate value at the two ends of top scope to select, carbonization temperature can be selected 300 ℃ or 500 ℃ or 800 ℃, and carbonization time can be selected 40 minutes or 2 hours or 4 hours; Carbonized material after charing heat material is directly sent into the activation converter carry out activation treatment, wherein activation temperature is 600 ~ 1200 ℃, soak time is 4 ~ 24 hours, activation temperature and soak time can be selected endpoint value and the intermediate value of top scope according to different operating modes such as the size of carbonized material and raw material, finished product requirements, can select 600 ℃ or 800 ℃ or 1200 ℃ as activation temperature, soak time can be selected 4 hours or 15 hours or 24 hours; Sending into activated material all, mixed cooling preparer is cooled to 40 ~ 80 ℃, can be cooled to 40 ℃ or 60 ℃ or 80 ℃ as activated material, and to add weight percent be that 0.05% or 3% or 5% sodium hydroxide or potassium hydroxide or ammoniacal liquor or urea carry out modulation treatment; The charcoal crude granule that obtains after the cooling modulation sieved with screening plant pack, obtain carbon product.
Embodiment 2:
Employed contenting carbon material was that blue charcoal is the mixture that 70:30 mixes with coke powder according to weight percent when present embodiment only was to make powdered carbon with the difference of embodiment 1; Perhaps employed contenting carbon material is that bituminous coal, blue charcoal are the mixture that 50:30:20 mixes with coke powder according to weight percent; Perhaps employed contenting carbon material is that the charing wood chip is the mixture that 60:40 mixes with coke powder according to weight percent; 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 can pass through 200 eye mesh screens.Employed tackiness agent is that tar is the mixture that 80:20 mixes with pitch according to weight percent; Be mixture that 90:10 mix with pitch according to weight percent for starch perhaps; Be mixture that 90:10 mix with pitch according to weight percent for resin perhaps.
Above-described embodiment is described preferred implementation of the present utility model; be not that scope of the present utility model is limited; under the prerequisite that does not break away from the utility model design spirit; various distortion and improvement that those of ordinary skills make the technical solution of the utility model all should fall in the definite protection domain of the utility model claims.
Claims (3)
1. a clean energy-saving is made the system of 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 mix 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) also is 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 the opening for feed that all mixes cooling preparer (10); the described cooling preparer (10) that all mixes is connected with screening plant (11); the tail gas outlet of described charing converter (5) and activation converter (6) is connected with the inlet mouth of tail gas burning furnace (7); 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 blast import of drying unit (4); the air outlet of described drying unit (4) is communicated with atmosphere; the vapour outlet that described waste heat boiler (8) produces is connected with the steam-in of activation converter (6) and charing converter (5) respectively; described tablets press (3); charing converter (5); be provided with cleaning apparatus (13) on the screening plant (11); described tablets press (3); the air outlet of the cleaning apparatus (13) of charing converter (5) and screening plant (11) all is connected with the inlet mouth of tail gas burning furnace (7); 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 mixing cooled off the below that preparer (10) is positioned at charing converter (5), and described screening plant (11) is positioned at the below of all mixing cooling preparer (10).
2. a kind of clean energy-saving according to claim 1 is made the system of carbon product, it is characterized in that: also comprise powdered carbon storage tank (14), material-compound tank (15) and tackiness agent jar (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), the discharge port tackiness agent blend tank (12) of described material-compound tank (15) and tackiness agent jar (16) is connected, and 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).
3. a kind of clean energy-saving according to claim 2 is made 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 first rotary conveyor (20), and the discharge port of described drying unit (4) is connected with the opening for feed of charing converter (5) by second rotary conveyor (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200826991U CN203144112U (en) | 2013-02-22 | 2013-02-22 | System for manufacturing carbon products in clean and energy-saving manner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200826991U CN203144112U (en) | 2013-02-22 | 2013-02-22 | System for manufacturing carbon products in clean and energy-saving manner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203144112U true CN203144112U (en) | 2013-08-21 |
Family
ID=48971656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013200826991U Expired - Fee Related CN203144112U (en) | 2013-02-22 | 2013-02-22 | System for manufacturing carbon products in clean and energy-saving manner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203144112U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103112841A (en) * | 2013-02-22 | 2013-05-22 | 邹炎 | Process and system for manufacturing carbon product in clean and energy-saving manner |
-
2013
- 2013-02-22 CN CN2013200826991U patent/CN203144112U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103112841A (en) * | 2013-02-22 | 2013-05-22 | 邹炎 | Process and system for manufacturing carbon product in clean and energy-saving manner |
| CN103112841B (en) * | 2013-02-22 | 2015-08-26 | 邹炎 | A kind of clean energy-saving manufactures technique and the system of carbon product |
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 | |
| CN103708452B (en) | A kind of autothermal continuously carbonizing activation working method of biomass and device thereof | |
| WO2008046254A1 (en) | A coal briquette used for gasification, process for producing the same and use thereof | |
| CN203683345U (en) | System for drying domestic sludge by using afterheat of dry process cement kiln and carrying out direct blending combustion treatment | |
| CN102258923A (en) | Method for recycling and reusing tail gas of calcium carbide furnace | |
| CN103922333B (en) | The oxygen carbonization pretreatment system prepared for active carbon from coal | |
| CN101738061A (en) | Kiln afterheat regeneration and drying process and device | |
| CN103112841B (en) | A kind of clean energy-saving manufactures technique and the system of carbon product | |
| CN101886811A (en) | Method for coprocessing sludge with high moisture content by novel dry-process rotary kiln | |
| CN104164244A (en) | Coal full-grain size grading pyrolysis and active coke preparation coupling process and system in coal gas circulating | |
| CN205079246U (en) | Device is used multipurposely to rice husk carbomorphism tail gas | |
| CN116147371A (en) | System and method for improving substitution rate of fossil fuel in cement industry | |
| CN203144112U (en) | System for manufacturing carbon products in clean and energy-saving manner | |
| CN206832029U (en) | The equipment that cement kiln head is burnt using biomass fuel catalysis | |
| CN203866039U (en) | Oxidizing and carbonizing pretreatment system for preparing coal-based activated carbon | |
| CN211814179U (en) | External combustion type limestone decomposition kiln equipment | |
| CN204039334U (en) | Coal gas circulation coal wholegrain radial sector pyrolysis coupling Active coke preparation system | |
| CN204434293U (en) | Prepare the system of calcium carbide | |
| CN203545892U (en) | Cement raw meal preheating and predecomposition device | |
| CN112856455A (en) | High-nitrogen high-sulfur colloidal asphaltene hazardous waste gas gasification incineration system and method | |
| CN205907226U (en) | Coal system gas fly ash treatment system | |
| CN202829612U (en) | Novel closed functional type production system of light calcium carbonate | |
| CN202193731U (en) | Flue gas waste heat double-circulating gas burning lime kiln | |
| CN107056106B (en) | Suspension catalytic oxidation flameless combustion device for wet biomass fuel |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20130821 Termination date: 20200222 |