CN101085677B - Bamboo charcoal activation producing process - Google Patents
Bamboo charcoal activation producing process Download PDFInfo
- Publication number
- CN101085677B CN101085677B CN2007100041459A CN200710004145A CN101085677B CN 101085677 B CN101085677 B CN 101085677B CN 2007100041459 A CN2007100041459 A CN 2007100041459A CN 200710004145 A CN200710004145 A CN 200710004145A CN 101085677 B CN101085677 B CN 101085677B
- Authority
- CN
- China
- Prior art keywords
- kiln
- bamboo charcoal
- steam
- wicket
- bamboo
- 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 invention relates to a process of producing bamboo activated carbon. It comprises following steps: selecting raw material, placing raw material in furnace, smoking and dehydrating, dry distilling and charring, refining, spraying steam and sealing furnace. The processes of smoking and carbonizing clear bamboo charcoal micro-pore, increase absorption and conductivity for bamboo charcoal. The invention is characterized by simple process, low cost, easy got raw material, high recovery rate, no pollution during producing process and natural product.
Description
Technical field
The present invention relates to a kind of technology of making charcoal, relate in particular to a kind of production technique of firing bamboo matter carbon activityization.
Background technology
Touching gac in the actual life, is raw material with the charcoal mainly, by secondary combustion, utilizes the stack gas activation, from timber to the black wood charcoal, utilization ratio has only 28%, and in second time reactivation process, a large amount of charcoal molecules are run away, and per three tons of charcoals can only reclaim one ton of gac, and the resource consumption is too big.Have kind of a chemical method to produce gac, the rate of recovery is slightly high, but the contaminated wastewater of producing is serious, influences environment protection.The application for a patent for invention of application number 98115886.2 by retrieval, a kind of production technique of bamboo charcoal is disclosed, but it lacks special sensitization production technique, so every performance index of this bamboo charcoal such as wettability power, deodorizing capability, screening ability and barbecue performance are all good not as the bamboo charcoal after the sensitization.
Summary of the invention
The present invention is directed to the above deficiency of prior art, and provide a kind of production technique simple, pollution-free, the bamboo matter carbon activity production technique that every performance index energy and wood activated charcoal match in excellence or beauty.
Purpose of the present invention, adopt following method to realize:
A kind of process for preparing activated carbon from bamboo is to comprise following production process:
1, material choice operation: mao bamboon is sawn into thick bamboo tube, and the back of drying in the shade is stand-by;
2, raw material loading of kiln operation: bamboo mao bamboon tube is loaded in the kiln according to certain rules, and the sealing wicket stays a burning osculum;
3, smoke the cigarette dehydration procedure:, kiln temperature is controlled at 25 ℃ in the igniting of burning osculum--105 ℃, steam cigarette dehydration 6--10 days with flue gas: '
4, dry distillation charring operation: be warming up to 150 ℃ in the kiln--about 300 ℃, bamboo charcoal is dry distillation charring under the state of partial vacuum, keeps 4 days:
5, refining procedure: slightly open wicket, increase oxygen supply, make to be warmed up to 700 ℃ in the kiln--1000 ℃,, kept 1 hour;
6, sensitization operation: establish gas orifice in the wicket middle and lower part, toward the interior water spray of kiln steam, seal wicket and chimney again with special steam generator;
7, envelope firer preface: with the bamboo charcoal after jet at kiln inner sealing kiln discharge after 4 days.
The present invention compared with prior art, smoke the activated carbon from bamboo that cigarette method and partial vacuum sensitization technology are fired owing to adopted, make bamboo charcoal physically activated thoroughly, mediation has also enlarged the bamboo charcoal micropore, increased the specific surface area of bamboo charcoal significantly, bringing up to 700-900 square centimeter/gram by original 192--360 square centimeter/gram, is 2--3 times of prior art.The activated technology of bamboo charcoal has strengthened the energy of charcoal molecule, has fundamentally improved moisture absorption, the deodorizing capability of bamboo charcoal, and every performance index energy and wood activated charcoal match in excellence or beauty, and technology is simple, and is with low cost, draws materials easily, rate of recovery height, production process is pollution-free, is the pure natural environment protection product.
Specific implementation method
Production technique of the present invention comprises following several process
One, material choice operation: adopt the 5-8 bamboo mao bamboon in age, be sawn into 2-2.5 rice Long Circle thick bamboo tube, the loading of kiln in 4 days of drying in the shade:
Two, raw material loading of kiln operation: according to diameter, from the inside to surface, interior thick outer thin, standing upside down is loaded in the kiln with circular thick bamboo tube, and the sealing wicket stays a little burning to steam mouth;
Three, smoke the cigarette dehydration procedure: advancing the quirk fuel combustion, temperature is at 25 ℃ in the control--105 ℃ (about), smoke the cigarette 8 day time of dehydration with stack gas;
Four, dry distillation charring operation: the former bamboo after last operation, its moisture content are all discharged, and continue to be warmed up to 150 ℃ this moment--and 300 ℃, bamboo charcoal carries out dry distillation charring under the state of partial vacuum, kept 4 days, this moment, kiln top smoke outlet was discharged clear cigarette, the complete charing of mao bamboon in the expression kiln;
Five, refining procedure: the manual labour wicket rises to 700--800 ℃ with kiln temperature, and the charcoal molecular aggregates in the bamboo charcoal is tightened, and increases oxygen supply from top to bottom, and the kiln temperature sharply rises to about 900 ℃, and visual inspection has the blue flame wriggling to rise, and keeps 30 minutes;
Six, sensitization operation: after treating that the charcoal molecule is assembled deflation fully, open the gas orifice of wicket middle and lower part, gas orifice is the 500-550 millimeter at the bottom of kiln, spray a small amount of water vapor to gas orifice earlier with electric heating steam generator, blue flame on the bamboo charcoal is progressively desalinated until cannot see, strengthen jet amount afterwards gradually, vapor pressure<the 0.11Mpa of vapour generator, steam production is at 8-10kg, and sprays into the quantity of steam control of the 1kg left and right sides by every cubic metre of bamboo charcoal, steam from the rapid ascension of kiln side to the top, become high-temperature steam again under main header casing, kiln words spoken by an actor from offstage mist is filled the air, and bamboo charcoal is among the complete anaerobic vacuum, seals wicket and chimney this moment immediately;
Seven: envelope firer preface: the bamboo charcoal that will spray behind the steam goes out charcoal at the kiln inner sealing about 4 days.
Claims (1)
1. bamboo charcoal activation producing process is characterized in that comprising following production process:
(1) material choice operation: mao bamboon is sawn into thick bamboo tube, and the back of drying in the shade is stand-by;
(2) raw material loading of kiln operation: the mao bamboon tube is loaded in the kiln according to certain rules, and the sealing wicket stays a burning osculum;
(3) smoke the cigarette dehydration procedure:, kiln temperature is controlled at 25 ℃ in the igniting of burning osculum--about 105 ℃, steam cigarette dehydration 6--10 days with flue gas;
(4) dry distillation charring operation: be warming up to 150 ℃ in the kiln--about 300 ℃, bamboo charcoal is dry distillation charring under the state of partial vacuum, keeps 4 days:
(5) refining procedure: open wicket, be warmed up to 700 ℃ in the kiln--1000 ℃, increase oxygen supply, kept 1 hour:
(6) sensitization operation: open the wicket gas orifice, toward the interior water spray of kiln steam, gas orifice is the 500-550 millimeter at the bottom of kiln, spray a small amount of water vapor to gas orifice earlier with electric heating steam generator, blue flame on the bamboo charcoal is progressively desalinated until cannot see, strengthen jet amount afterwards gradually, vapor pressure<the 0.11Mpa of vapour generator, steam production is at 8-10kg, and spraying into the control of 1kg left and right sides quantity of steam by every cubic metre of bamboo charcoal, steam to the top, becomes high-temperature steam from the rapid ascension of kiln side again under main header casing, bamboo charcoal is among the complete anaerobic vacuum, seals wicket and chimney this moment again;
(7) envelope firer preface: with the bamboo charcoal after jet at kiln inner sealing kiln discharge after 4 days.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2007100041459A CN101085677B (en) | 2007-01-01 | 2007-01-01 | Bamboo charcoal activation producing process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2007100041459A CN101085677B (en) | 2007-01-01 | 2007-01-01 | Bamboo charcoal activation producing process |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101085677A CN101085677A (en) | 2007-12-12 |
CN101085677B true CN101085677B (en) | 2011-03-16 |
Family
ID=38936881
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2007100041459A Expired - Fee Related CN101085677B (en) | 2007-01-01 | 2007-01-01 | Bamboo charcoal activation producing process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101085677B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103435040A (en) * | 2013-09-09 | 2013-12-11 | 武汉大学 | Bamboo integrated activated carbon based pollution adsorption purifying method and applications thereof |
CN103466617B (en) * | 2013-09-18 | 2016-06-29 | 韦仲华 | A kind of preparation method of High-temperature crystallite bamboo charcoal |
CN110202655A (en) * | 2019-07-16 | 2019-09-06 | 龙泉市众伟竹木有限公司 | A kind of moso bamboo discongests the production method of piece |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1382625A (en) * | 2002-06-09 | 2002-12-04 | 陈文照 | Process for preparing activated carbon from bamboo |
-
2007
- 2007-01-01 CN CN2007100041459A patent/CN101085677B/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1382625A (en) * | 2002-06-09 | 2002-12-04 | 陈文照 | Process for preparing activated carbon from bamboo |
Also Published As
Publication number | Publication date |
---|---|
CN101085677A (en) | 2007-12-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101921604B (en) | Dry distillation charring method for bamboos | |
CN103693642B (en) | Prepare method and the production equipment thereof of bamboo matrix activated carbon | |
CN102161897B (en) | Method for preparing charcoal activated carbon flammable gas biological oil by utilizing crop straws | |
CN105948039B (en) | A kind of system and method for giantreed production activated carbon coproduction power generation | |
CN101885487A (en) | Device and method for continuously preparing active carbon by biomass in bulk | |
CN205235984U (en) | Low energy consumption saturation activated carbon regeneration system | |
CN1803981A (en) | Method for manufacturing machine processed charcoal by utilizing Chinese medicinal or herbal drug to extract solid waste | |
CN105439140A (en) | System for preparing activated carbon and preparation method thereof | |
CN101085677B (en) | Bamboo charcoal activation producing process | |
CN102942963A (en) | Production process of biomass gasifying and carbonizing material | |
CN103484138B (en) | Manufacturing process and equipment of bamboo charcoal | |
CN105316068A (en) | Health-type charcoal for indoor warming | |
CN1382625A (en) | Process for preparing activated carbon from bamboo | |
CN105542870B (en) | It is a kind of to carry out charcoal, air-liquid, the system and production method of oily coproduction using biomass | |
CN102206498A (en) | Method for firing high-density bamboo charcoal by using medium-small diameter bamboos | |
CN201737705U (en) | Device for batch and continuous preparation of activated charcoal by biomass | |
CN106552612A (en) | A kind of microwave improves the method that activity of bamboo charcoal increases absorption property | |
CN201587862U (en) | Microwave heating rotary activation furnace for activated carbon production in garbage microwave pyrolysis | |
CN101020344A (en) | Process and apparatus for producing stalk honeycomb briquet | |
CN203530160U (en) | Device for recycling household waste wood and waste paper through ozone odor removing treatment | |
CN105329891A (en) | Bamboo charcoal activation production technology | |
CN106809833A (en) | Bamboo charcoal activation producing process | |
CN105399092A (en) | Bamboo charcoal activation production process | |
CN204372935U (en) | The destructive distillation device of organic solid castoff harmless treatment | |
CN103466614B (en) | Activated carbon production technology |
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 |
Granted publication date: 20110316 Termination date: 20160101 |
|
EXPY | Termination of patent right or utility model |