CN203128210U - Active carbon producing equipment - Google Patents
Active carbon producing equipment Download PDFInfo
- Publication number
- CN203128210U CN203128210U CN201320128700XU CN201320128700U CN203128210U CN 203128210 U CN203128210 U CN 203128210U CN 201320128700X U CN201320128700X U CN 201320128700XU CN 201320128700 U CN201320128700 U CN 201320128700U CN 203128210 U CN203128210 U CN 203128210U
- Authority
- CN
- China
- Prior art keywords
- collector
- carbon production
- activated carbon
- condensable gases
- ball valve
- 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 - Lifetime
Links
Images
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
The utility model relates to active carbon producing equipment. The active carbon producing equipment comprises a steam generating device (1), a high-temperature pyrolysis reaction device (2) and an integrated condensing device (3) which are connected in sequence; a condensate collector (306) and an un-condensable gas collector (309) are arranged in the integrated condensing device (3); and the un-condensable gas collector (309) is communicated with the high-temperature pyrolysis reaction device (2). By adopting the equipment, waste smoke generated during the active carbon production process is recycled and developed during active carbon production, and therefore, the additional value of the active carbon production is improved, an energy source is saved, the consumption of raw materials is reduced, and the problem of environment pollution in the active carbon production process is solved.
Description
Technical field
The utility model relates to the Activated Carbon Production field, particularly relates to a kind of Activated Carbon Production equipment.
Background technology
Gac (Activated Carbon) is a class microcrystalline carbon that is black, the prosperity of internal voids structure, surface-area height, high adsorption capacity by the outward appearance of carbonaceous material manufacturing.Gac has certain chemical stability, physical strength and acid and alkali-resistance, key property such as heat-resisting, and it has been obtained extensively and important use at numerous areas such as food, chemical industry, national defence, medicine, environmental protection and agriculturals.At present, the production method of gac mainly contains chemical activation method, physical activation method and chemical physics activation method.Physical activation method prepares gac mainly with oxidizing gas (CO
2, H
2O, air etc.) be activator.The carbon atom reaction of activator and raw material inside generates gas and overflows, and will form hole at the carbon atom place like this, after the carbon atom of q.s and the activator reaction, will produce a large amount of microvoid structures.Chemical activation is the process that forms microvoid structure with chemical reagent and starting material through crosslinked or polycondensation.Chemical activation is more with short production cycle than physically activated, and technical maturity.At present, Chang Yong activator has H
3PO
4, NaOH, ZnCl
2Deng.Chemistry-physical union activation method is the advantage of comprehensive physics and chemical activation method, and preparation high absorption property gac, but the present technical weak point that exists need further to study dependent interaction mechanism between them, also will develop new technical equipment.
The major equipment of producing gac has the rake stove, multi-tube furnace, Stepple furnace, rotary kiln, smouldering furnace, fluidizing furnace etc., different equipment in producing the gac process to the requirement of raw material, the specification of body of heater, the expense of investment and the performance of final activated carbon product had different relative merits, but their overall characteristics are that the power consumption of Activated Carbon Production process is high, produce a large amount of high temperature and waste heat after the pyroreaction, flue dust and obnoxious flavour etc., the processing costs height, difficulty is big, if directly be discharged in the atmosphere by chimney, so not only reduce capacity usage ratio, caused environmental pollution simultaneously.
Because the defective that above-mentioned existing Activated Carbon Production equipment exists, the inventor is based on being engaged in practical experience and the expertise that this type of product design manufacturing is enriched for many years, and the utilization of cooperation scientific principle, actively studied innovation, in the hope of founding a kind of new Activated Carbon Production equipment, can improve general existing equipment, make it have more practicality.Through constantly research, design, and through after studying sample and improvement repeatedly, create the utility model that has practical value finally.
Summary of the invention
The utility model is at the deficiencies in the prior art, and a kind of equipment of environment-friendly and energy-efficient Activated Carbon Production is designed in use heat engineering, environmental science, Computer Control Technology synthetic study.This equipment design advanced person, technology rationally, operational safety, level of automation height; Carry out recycle and exploitation to producing the useless flue gas that produces in the gac process, save energy reduces raw materials consumption, and the control environmental pollution is played a good role.
According to the Activated Carbon Production equipment that the utility model proposes, it comprises: steam-generating installation, high temperature pyrolysis reaction unit, integrated form condensing works, and above various device is interconnected successively; Be provided with condensate collector and non-condensable gases collector in the integrated form condensing works, and this not the condensable gases collector communicate with this high temperature pyrolysis reaction unit.
More preferably, this condensate collector is provided with air valve, and it is regulated and control by air valve, via scrubbing bottle with this not the condensable gases collector be connected; So arrange, the useless flue gas that produces in the condensate collector can be collected, reduce the quantity discharged in the environment.
Aforesaid steam-generating installation can comprise vapour generator, and this vapour generator is connected with ball valve II in this high temperature pyrolysis reaction unit via safety valve, ball valve I, reducing valve, first tensimeter, under meter, the first steel wire corrugated tube successively, but is not limited thereto.
Further; this vapour generator finally is connected with rotary kiln in this high temperature pyrolysis reaction unit via four-way valve; this not the condensable gases collector be connected with this four-way valve via vacuum pump, ball valve III, last end of this four-way valve (namely still being in an end of not-connected status) is connected with the protective gas storage tank via ball valve IV, second tensimeter successively.This rotary kiln can be produced gac equipment by other and be substituted, for example rake stove, multi-tube furnace, Stepple furnace, smouldering furnace, fluidizing furnace etc.
Further, this rotary kiln via the condensation rotary sleeve, connect clip soon, the second steel wire corrugated tube is connected with the integrated form cooling water tank of this integrated condensing works, the bottom of this integrated form cooling water tank and this condensate collector, this not the condensable gases collector be connected respectively.
By technique scheme, the utility model Activated Carbon Production equipment has following advantage and beneficial effect at least:
(1) this equipment can prepare with materials such as agriculture and forestry organic waste material, coke, refinery coke, various nutshells and is the gac of raw material and is used for exotic materials under the particular atmosphere protection.
(2) expanded equipment and the technology of producing gac; equipment and process system that the cleaning action charcoal is produced have been formed; in the preparation gac, wood gas, wood vinegar and tar have been collected; and the not condensable gases that recycling self produces is as the protective gas in the reaction process; improve the added value of producing gac, solved the problem of environmental pollution in the Activated Carbon Production process.
(3) this equipment type of heating is that the self-circulation type type of heating combines in outside boosting and the material reaction process, and providing of thermal source in the material reaction process effectively is provided, has reduced energy consumption.
(4) wood vinegar by this device fabrication also is vegetable acid, contain multiple organic mixtures such as acid, alcohol, phenol, ketone, have multiple effects such as soil disinfection, sterilization, promotion plant-growth, weeding, pest control and anticorrosion and deodorizing, can be widely used in chemical industry, forestry, agricultural, livestock industry, food-processing industry and medical and health industry.The wood gas that produces is more superior than general solid fuel, and combustion processes is easily reconciled, and burning is complete, and the flame temperature height does not have lime-ash, and is easy to carry.The tar that produces can obtain multiple product after processing.As anti-poly-agent, oxidation inhibitor, creosote, creosote, flotation oil, syntannin, wood pitch etc.These products are widely used in multiple industrial sectors such as synthetic rubber, petrochemical complex, chemical industry, mining, process hides, medicine, building.
Above-mentioned explanation only is the general introduction of technical solutions of the utility model, for can clearer understanding technique means of the present utility model, and can be implemented according to the content of specification sheets, and for above-mentioned and other purposes, feature and advantage of the present utility model can be become apparent, below especially exemplified by preferred embodiment, and conjunction with figs., be described in detail as follows.
Description of drawings
Fig. 1 is Activated Carbon Production equipment essentially consist synoptic diagram among the utility model one embodiment.
Fig. 2 is the process flow sheet that gac among the utility model one embodiment, wood vinegar, tar and wood gas are produced.
1: steam generating device
11: full-automatic electric heating steam generator 12: safety valve
13: ball valve I 14: reducing valve
17: the first steel wire corrugated tubes
2: the high temperature pyrolysis reaction unit
21: ball valve II 22: four-way valve
23: rotary kiln 24: ball valve IV
3: the integrated form condensing works
301: condensation rotary sleeve 302: connect clip soon
303: the second steel wire corrugated tubes 304: integrated form cooling water tank
305: air valve 306: condensate collector
307,308: scrubbing bottle 309: condensable gases collector not
310: vacuum pump 311: ball valve III
Embodiment
Be to reach technique means and the effect that predetermined goal of the invention is taked for further setting forth the utility model, below in conjunction with accompanying drawing and preferred embodiment, to according to its embodiment of Activated Carbon Production equipment, structure, feature and the effect thereof that the utility model proposes, describe in detail as after.
Embodiment 1
Present embodiment is used for describing in detail the equipment of this Activated Carbon Production of the present utility model.
By shown in Figure 1, a kind of equipment of Activated Carbon Production comprises steam generating device 1, high temperature pyrolysis reaction unit 2, integrated form condensing works 3, and above various device is interconnected successively.
Steam-generating installation 1 mainly contains full-automatic electric heating steam generator 11, the steam that produces forms pressure and the metastable steam of flow through safety valve 12, ball valve I13, reducing valve 14, first tensimeter 15, under meter 16, links to each other with ball valve II21 in the high temperature pyrolysis reaction unit 2 by the first steel wire corrugated tube 17; Steam enters in the rotary kiln 23 through the four-way valve 22 that links to each other with this ball valve II21 in the high temperature pyrolysis reaction unit 2, carries out the charcoal priming reaction with material; The high-temperature waste flue gas that produces in the reaction process, by condensation rotary sleeve 301 with connect clip 302 soon and introduced in the integrated form condensing workss 3 by the second steel wire corrugated tube 303, through integrated form cooling water tank 304, the material that can cool off is collected in condensate collector 306, when adopting lignocellulose to produce the raw material of gac, this condensation product further is separated into wood vinegar, tar; And when adopting other raw materials, this condensation product is tar; The useless flue gas of the small portion that produces in the condensate collector 306 after process scrubbing bottle 307,308 is handled, further is collected in not condensable gases collector 309 by air valve 305 regulation and control; Form a large amount of not condensable gases in the production process, be collected in not in the condensable gases collector 309, this not the part in the condensable gases collector 309 not condensable gases by vacuum pump 310, send in the rotary kiln 23 through ball valve III311, four-way valve 22, as the protective gas in the charcoal reactivation process, a part is stored in the gas tank as burning gas in addition; Protective gas in the protective gas storage tank 26 through second tensimeter 25 and ball valve IV24, enters in the rotary kiln 23 by four-way valve 22, as the protective gas of material reaction initial period.
Following examples 2-6 is used for describing in detail the method that aforesaid device is produced gac, wood vinegar, tar and wood gas of using, following examples are that raw material such as the technology wood chip of producing gac with lignocellulose are that example is specifically described, but scope of the present utility model is not as limit, for Activated Carbon Production equipment of the present utility model and the Activated Carbon Production method of using this equipment raw material is not particularly limited, only need ask raw material when using this device fabrication wood vinegar or wood gas is lignocellulose raw material.
See also Fig. 1 and Fig. 2.
(1) raw material is prepared and the program setting stage.The technology wood chip that processes is added in the rotary kiln 23, close charging opening, temperature rise rate and the temperature range of rotary kiln 23 is set.Wherein, the fs: 10 ℃/min of temperature rise rate, 0～600 ℃ of temperature range; Subordinate phase: 10 ℃/min of temperature rise rate, 600～1200 ℃ of temperature ranges; Phase III: stop heating, start cooling process.
(2) charcoal activation and reactant collection phase.Open ball valve IV24; close ball valve II21; open the protective gas that from protective gas storage tank 26, enters; high-temperature waste flue gas with the generation of reaction fs; by condensation rotary sleeve 301 with connect clip 302 soon and introduce integrated form condensing workss 3 by the second steel wire corrugated tube 303; through integrated form cooling water tank 304; the material that can cool off is collected in condensate collector 306; with the not condensable gases that finally forms; be collected in not in the condensable gases collector 309; a part is by vacuum pump 310; ball valve III311 sends in the rotary kiln 23 through four-way valve 22, as the protective gas in the charcoal reactivation process.After reaction enters subordinate phase, close ball valve IV24, stop from four-way valve 22, to enter the protective gas of body of heater, open ball valve II21, start steam generating device, feed the gas activation agent, the maintenance vapor flow rate is 5kg/h, and the pressure that steams carries out the charcoal activation of subordinate phase less than 0.40MPa; After question response finishes, the reaction that enters the phase III.After reaction enters the phase III, stop to feed the gas activation agent, feed protective gas, stop heating, start cooling process.
(3) product is collected and post-processing stages.Cooled gac is taken out from the revolution boiler tube, after rinsing, screening, detection, pack; Condensation product is kept in Dark Place, as the new source material of derived product exploitation; Condensable gases is not collected in the tracheae, stores as burning gas.The yield of gac is 34% under this technology, and the yield of wood vinegar is 31%, and the tar yield is 12%, and the yield of wood gas is 23%.
(1) raw material is prepared and the program setting stage.The technology wood chip that processes is added in the rotary kiln 23, close charging opening, temperature rise rate and the temperature range of rotary kiln 23 is set.Wherein, the fs: 5 ℃/min of temperature rise rate, 0～500 ℃ of temperature range; Subordinate phase: 10 ℃/min of temperature rise rate, 500～1200 ℃ of temperature ranges; Phase III: stop heating, start cooling process.
(2) charcoal activation and reactant collection phase.Open ball valve IV24; close ball valve II21; open the protective gas that from protective gas storage tank 26, enters; high-temperature waste flue gas with the generation of reaction fs; by condensation rotary sleeve 301 with connect clip 302 soon and introduce integrated form condensing workss 3 by the second steel wire corrugated tube 303; through integrated form cooling water tank 304; the material that can cool off is collected in condensate collector 306; with the not condensable gases that finally forms; be collected in not in the condensable gases collector 309; this not the part in the condensable gases collector 309 not condensable gases by vacuum pump 310; ball valve III311 sends in the rotary kiln 23 through four-way valve 22, as the protective gas in the charcoal reactivation process.After reaction enters subordinate phase, close ball valve IV24, stop from four-way valve 22, to enter the protective gas of body of heater, open ball valve II21, start steam-generating installation, feed the gas activation agent, the maintenance vapor flow rate is 8kg/h, and the pressure that steams carries out the charcoal activation of subordinate phase less than 0.50MPa; After question response finishes, the reaction that enters the phase III.After reaction enters the phase III, stop to feed the gas activation agent, feed protective gas, stop heating, start cooling process.
(3) product is collected and post-processing stages.Cooled gac is taken out from the revolution boiler tube, after rinsing, screening, detection, pack; Condensation product is kept in Dark Place, as the new source material of derived product exploitation; Condensable gases is not collected in the tracheae, stores as burning gas.The yield of gac is 32% under this technology, and the yield of wood vinegar is 35%, and the tar yield is 14%, and the yield of wood gas is 19%.
Embodiment 4
(1) raw material is prepared and the program setting stage.The technology wood chip that processes is added in the rotary kiln 23, close charging opening, temperature rise rate and the temperature range of rotary kiln 23 is set.Wherein, the fs: 15 ℃/min of temperature rise rate, 0～600 ℃ of temperature range; Subordinate phase: 15 ℃/min of temperature rise rate, 600～1200 ℃ of temperature ranges; Phase III: stop heating, start cooling process.
(2) charcoal activation and reactant collection phase.Open ball valve IV24; close ball valve II21; open the protective gas that from protective gas storage tank 26, enters; high-temperature waste flue gas with the generation of reaction fs; by condensation rotary sleeve 301 with connect clip 302 soon and introduce integrated form condensing workss 3 by the second steel wire corrugated tube 303; through integrated form cooling water tank 304; the material that can cool off is collected in condensate collector 306; with the not condensable gases that finally forms; be collected in not in the condensable gases collector 309; this not the part in the condensable gases collector 309 not condensable gases by vacuum pump 310; ball valve III311 sends in the rotary kiln 23 through four-way valve 22, as the protective gas in the charcoal reactivation process.After reaction enters subordinate phase, close ball valve IV24, stop from four-way valve 22, to enter the protective gas of body of heater, open ball valve II21, start steam-generating installation, feed the gas activation agent, the maintenance vapor flow rate is 3kg/h, and the pressure that steams carries out the charcoal activation of subordinate phase less than 0.50MPa; After question response finishes, the reaction that enters the phase III.After reaction enters the phase III, stop to feed the gas activation agent, feed protective gas, stop heating, start cooling process.
(3) product is collected and post-processing stages.Cooled gac is taken out from the revolution boiler tube, after rinsing, screening, detection, pack; Condensation product is kept in Dark Place, as the new source material of derived product exploitation; Condensable gases is not collected in the tracheae, stores as burning gas.The yield of gac is 33.5% under this technology, and the yield of wood vinegar is 30.5%, and the tar yield is 16%, and the yield of wood gas is 20%.
Embodiment 5
(1) raw material is prepared and the program setting stage.The technology wood chip that processes is added in the rotary kiln 23, close charging opening, temperature rise rate and the temperature range of rotary kiln 23 is set.Wherein, the fs: 1 ℃/min of temperature rise rate, 0～500 ℃ of temperature range; Subordinate phase: 1 ℃/min of temperature rise rate, 500～1200 ℃ of temperature ranges; Phase III: stop heating, start cooling process.
(2) charcoal activation and reactant collection phase.Open ball valve IV24; close ball valve II21; open the protective gas that from protective gas storage tank 26, enters; high-temperature waste flue gas with the generation of reaction fs; by condensation rotary sleeve 301 with connect clip 302 soon and introduce integrated form condensing workss 3 by the second steel wire corrugated tube 303; through integrated form cooling water tank 304; the material that can cool off is collected in condensate collector 306; with the not condensable gases that finally forms; be collected in not in the condensable gases collector 309; this not the part in the condensable gases collector 309 not condensable gases by vacuum pump 310; ball valve III311 sends in the rotary kiln 23 through four-way valve 22, as the protective gas in the charcoal reactivation process.After reaction enters subordinate phase, close ball valve IV24, stop from four-way valve 22, to enter the protective gas of body of heater, open ball valve II21, start steam-generating installation, feed the gas activation agent, the maintenance vapor flow rate is 4kg/h, and the pressure that steams carries out the charcoal activation of subordinate phase less than 0.50MPa; After question response finishes, the reaction that enters the phase III.After reaction enters the phase III, stop to feed the gas activation agent, feed protective gas, stop heating, start cooling process.
(3) product is collected and post-processing stages.Cooled gac is taken out from the revolution boiler tube, after rinsing, screening, detection, pack; Condensation product is kept in Dark Place, as the new source material of derived product exploitation; Condensable gases is not collected in the tracheae, stores as burning gas.The yield of gac is 29.5% under this technology, and the yield of wood vinegar is 34.5%, and the tar yield is 14.5%, and the yield of wood gas is 21.5%.
Embodiment 6
(1) raw material is prepared and the program setting stage.The technology wood chip that processes is added in the rotary kiln 23, close charging opening, temperature rise rate and the temperature range of rotary kiln 23 is set.Wherein, the fs: 1 ℃/min of temperature rise rate, 0～400 ℃ of temperature range; Subordinate phase: 10 ℃/min of temperature rise rate, 400～1200 ℃ of temperature ranges; Phase III: stop heating, start cooling process.
(2) charcoal activation and reactant collection phase.Open ball valve IV24; close ball valve II21; open the protective gas that from protective gas storage tank 26, enters; high-temperature waste flue gas with the generation of reaction fs; by condensation rotary sleeve 301 with connect clip 302 soon and introduce integrated form condensing workss 3 by the second steel wire corrugated tube 303; through integrated form cooling water tank 304; the material that can cool off is collected in condensate collector 306; with the not condensable gases that finally forms; be collected in not in the condensable gases collector 309; this not the part in the condensable gases collector 309 not condensable gases by vacuum pump 310; ball valve III311 sends in the rotary kiln 23 through four-way valve 22, as the protective gas in the charcoal reactivation process.After reaction enters subordinate phase, close ball valve IV24, stop from four-way valve 22, to enter the protective gas of body of heater, open ball valve II21, start steam generating device, feed the gas activation agent, the maintenance vapor flow rate is 10kg/h, the pressure that steams is 0～0.50MPa, carries out the charcoal activation of subordinate phase; After question response finishes, the reaction that enters the phase III.After reaction enters the phase III, stop to feed the gas activation agent, feed protective gas, stop heating, start cooling process.
(3) product is collected and post-processing stages.Cooled gac is taken out from the revolution boiler tube, after rinsing, screening, detection, pack; Condensation product is kept in Dark Place, as the new source material of derived product exploitation; Condensable gases is not collected in the tracheae, stores as burning gas.The yield of gac is 33% under this technology, and the yield of wood vinegar is 39%, and the tar yield is 11%, and the yield of wood gas is 16%.
In the previous embodiment, the steam production of vapour generator 11 is 0～80kg/h in the described steam-generating installation 1, and the pressure that steams is 0～0.50MPa; Safety valve 12 can be monitored the safety in production of vapour generator, prevents the unstable accident that normal atmosphere causes; Ball valve I13 can control the quantity of steam that enters next stage; The pressure range of reducing valve 14 is less than 0.50Mpa; the measurement range of first tensimeter 15 is 0～1.0Mpa; effectively protected under meter 16 by regulation and control reducing valve 14 and first tensimeter 15; prevent because the air pressure instability causes the destruction under meter; impel it to produce stable steam, carry out in order to follow-up reaction.
Four-way valve 22 in the described high temperature pyrolysis reaction unit 2 both can feed the not condensable gases that extraneous protective gas and id reaction produce at material at the charcoal activation stage, also can carry out the charcoal activation stage at material and feed the gas activation agent (as CO
2, H
2O, air etc.), consumption is 30～75kg/h; Material charcoal activation temperature is 200～1200 ℃ in the rotary kiln 23, and the reaction times is 1～6h.
Condensation rotary sleeve 301 in the described integrated form condensing works 3 both can reduce the temperature that enters the useless flue gas in the condensing works, prevented owing to too high effusion of useless flue-gas temperature, also can protect owing to the destruction of the too high formation of temperature to condensing works; The gas of condensable gases collection device collection is not mainly wood gas, both can be used as the protective gas in the charcoal reactivation process, can be used as clean fuel yet; The material that condensate collector is collected mainly contains wood vinegar, tar.
According to the gac of the utility model Activated Carbon Production equipment preparation, its performance index are compared with standard index and are listed in the table 1.
The detected result of the gac of table 1 application Activated Carbon Production equipment preparation of the present utility model and the synopsis of standard index
Standard index in the table is the Ministry of Chemical Industry of the People's Republic of China (PRC) that announces according to HG3-1290-80, and gac ministerial standard, detected result are the test event indexs that the utility model detects.Utilize the gac of Activated Carbon Production equipment preparation of the present utility model as can be seen from Table 1, the main performance index adsorptive capacity is greater than ministerial standard.Therefore, the technical process that use provided by the utility model Activated Carbon Production equipment of the present utility model prepares gac is perfect, and quality product meets the back and surpasses ministerial standard.
According to the wood vinegar of Activated Carbon Production equipment preparation of the present utility model, its character: pH is 1～3, and total acid content is 3%～14%, and density is: 1～2gmL
-1, refractive index is 1～42%, it is as follows that its wood vinegar chemical ingredients is carried out analytical results:
Table 2 wood vinegar stoste GC-MS Analysis of Chemical result
Tar according to Activated Carbon Production equipment preparation of the present utility model is the brown thick liquid, relative density (20 ℃) 0.8～1.2, viscosity Engler 240～300.
According to the wood gas of Activated Carbon Production equipment preparation of the present utility model, flame temperature is 600 ℃～1300 ℃.
The above, it only is preferred embodiment of the present utility model, be not that the utility model is done any pro forma restriction, though the utility model discloses as above with preferred embodiment, yet be not in order to limit the utility model, any those skilled in the art, in not breaking away from the technical solutions of the utility model scope, when the method that can utilize above-mentioned announcement and technology contents are made a little change or be modified to the equivalent embodiment of equivalent variations, in every case be the content that does not break away from technical solutions of the utility model, any simple modification that foundation technical spirit of the present utility model is done above embodiment, equivalent variations and modification all still belong in the scope of technical solutions of the utility model.
Claims (6)
1. Activated Carbon Production equipment is characterized in that it comprises: steam-generating installation (1), high temperature pyrolysis reaction unit (2), integrated form condensing works (3), and above various device is interconnected successively; Be provided with condensate collector (306) and condensable gases collector (309) not in the integrated form condensing works (3), and this not condensable gases collector (309) communicate with this high temperature pyrolysis reaction unit (2).
2. Activated Carbon Production equipment according to claim 1, it is characterized in that this condensate collector (306) is provided with air valve (305), this condensate collector (306) via scrubbing bottle (307,308) with this not condensable gases collector (309) be connected.
3. Activated Carbon Production equipment according to claim 1 and 2, it is characterized in that this steam-generating installation (1) comprises vapour generator (11), this vapour generator (11) is successively via safety valve (12), ball valve I(13), the ball valve II(21 in reducing valve (14), first tensimeter (15), under meter (16), the first steel wire corrugated tube (17) and this high temperature pyrolysis reaction unit (2)) be connected.
4. Activated Carbon Production equipment according to claim 3; it is characterized in that this vapour generator (11) finally is connected with rotary kiln (23) in this high temperature pyrolysis reaction unit (2) via four-way valve (22); this not condensable gases collector (309) via vacuum pump (310), ball valve III(311) be connected with this four-way valve (22), last end of this four-way valve is successively via ball valve IV(24), second tensimeter (25) is connected with protective gas storage tank (26).
5. Activated Carbon Production equipment according to claim 4, it is characterized in that this rotary kiln (23) via condensation rotary sleeve (301), connect clip (302) soon, the second steel wire corrugated tube (303) is connected with the integrated form cooling water tank (304) of this integrated condensing works (3), the bottom of this integrated form cooling water tank (304) and this condensate collector (306), this not condensable gases collector (309) be connected respectively.
6. according to claim 4 or 5 described Activated Carbon Production equipment, it is characterized in that this rotary kiln (23) is substituted by rake stove, multi-tube furnace, Stepple furnace, smouldering furnace or fluidizing furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320128700XU CN203128210U (en) | 2013-03-20 | 2013-03-20 | Active carbon producing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320128700XU CN203128210U (en) | 2013-03-20 | 2013-03-20 | Active carbon producing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203128210U true CN203128210U (en) | 2013-08-14 |
Family
ID=48936208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320128700XU Expired - Lifetime CN203128210U (en) | 2013-03-20 | 2013-03-20 | Active carbon producing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203128210U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2789699C1 (en) * | 2021-12-03 | 2023-02-07 | федеральное государственное бюджетное образовательное учреждение высшего образования "Казанский национальный исследовательский технологический университет" (ФГБОУ ВО "КНИТУ") | Method for production of activated carbon |
-
2013
- 2013-03-20 CN CN201320128700XU patent/CN203128210U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2789699C1 (en) * | 2021-12-03 | 2023-02-07 | федеральное государственное бюджетное образовательное учреждение высшего образования "Казанский национальный исследовательский технологический университет" (ФГБОУ ВО "КНИТУ") | Method for production of activated carbon |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103265026B (en) | Activated carbon production equipment and method for applying the equipment to production of activate carbon, pyroligneous liquor, tar and wood gas | |
| CN103359898B (en) | Method and apparatus for sludge deep treatment and resource utilization | |
| CN108913175B (en) | Combined cycle system for treating organic wastewater based on waste biomass catalytic pyrolysis products and use method thereof | |
| CN101191059B (en) | Dynamics gasification furnace and exhaust heat boiler composed by the same | |
| CN106746468A (en) | A kind of sludge treating system and handling process | |
| CN105368496A (en) | Process method for cogenerating electricity, charcoal, heat and fertilizer through gasified gas supply of biomass | |
| CN105368502B (en) | A kind of stalk fluidized gasification power generating simultaneously electricity, charcoal, the technique of heat | |
| CN105948039A (en) | System and method for producing activated carbon and cogenerating power by using Arundo donax Linn | |
| CN103274400B (en) | The method of gac is produced in the pyrolysis of salix monogolica branch wood | |
| CN103274399B (en) | Method for producing active carbon by pyrolysing pepper branches | |
| CN204607939U (en) | The combustion and segmented inverting biological charcoal/steam co-producing device of biomass pyrogenation gasification | |
| CN104832938A (en) | High-temperature flue gas recovery and heat energy utilization device and method for bamboo charcoal pyrolysis process | |
| CN205774358U (en) | A kind of carbonaceous organic material continuous pyrolysis purifies the system of CO fuel gas | |
| CN101270289A (en) | Technique for producing wood tar | |
| CN206692598U (en) | A kind of worn-out agricultural film process in plastics device | |
| CN203128210U (en) | Active carbon producing equipment | |
| CN206276399U (en) | A kind of preparation system of giantreed biomass carbon adsorbent | |
| CN109054877A (en) | A kind of biomass carbonated equipment and charing method | |
| CN106378348B (en) | Treatment of wastes produced and resource utilization method | |
| CN108485689A (en) | A kind of device and method that lignite is reacted with biomass microwave copyrolysis | |
| CN210855995U (en) | Vertical living beings charcoal gas-liquid-oil coproduction dry distillation device of electrical heating formula | |
| CN206721114U (en) | Straw recycles chemical plant installations | |
| CN106495153A (en) | The method of production material with carbon element | |
| CN202581422U (en) | Gasified gas furnace with environmental friendliness and high thermal effect | |
| CN103361090A (en) | Method for preparation of tar by microwave pyrolysis of kitchen garbage |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130814 |