CN204981748U - Quick air -cooled type living beings anaerobic low temperature pyrolysis result piece -rate system - Google Patents
Quick air -cooled type living beings anaerobic low temperature pyrolysis result piece -rate system Download PDFInfo
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- CN204981748U CN204981748U CN201520124243.6U CN201520124243U CN204981748U CN 204981748 U CN204981748 U CN 204981748U CN 201520124243 U CN201520124243 U CN 201520124243U CN 204981748 U CN204981748 U CN 204981748U
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- gas
- liquid separator
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Separation Of Gases By Adsorption (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model relates to a quick air -cooled type living beings anaerobic low temperature pyrolysis result piece -rate system, including the gas retort, pipe connection one -level forced air cooler is passed through to the gas outlet of gas retort, a vapour and liquid separator is connected to one -level forced air cooler's gas outlet, a vapour and liquid separator's bottom exit linkage wood tar liquid storage pot, second grade water chiller is connected to a vapour and liquid separator's the end of giving vent to anger, the 2nd vapour and liquid separator is connected to second grade water chiller's the end of giving vent to anger, the pyrolkigneous liquid liquid storage pot is connected to a vapour and liquid separator's bottom, the active carbon adsorption jar is connected to the 2nd vapour and liquid separator's the end of giving vent to anger, roots's fan is connected to the end of giving vent to anger of active carbon adsorption jar, the gas gas holder is connected to roots's fan. The utility model discloses a second grade cooling and grade separation realize the high efficiency separation of wood tar with the pyrolkigneous liquid, relict acid aerial fog in the adsorbed gas of trafficability characteristic charcoal adsorption tanks, and the purification mist obtains the combustible gas mixture that pure degree is high, entire system compact structure, area is little, and is with low costs.
Description
Technical field
The utility model belongs to biomass processing field, is specifically related to a kind of fast wind cold mould biomass anaerobic low-temperature pyrolysis product separation system.
Background technology
The low-temperature pyrolysis of biomass anaerobic manufactures clean fuel gas and other economic product has enormous benefits to improvement environment and utilization of waste material, and substantially do not produce secondary pollution, destructive distillation product is all converted into product, substantially produces without waste gas, waste water, waste residue.Straw, pruning fruit tree branch, the biomass wastes such as waste and old wood are fully utilized, and for minimizing carbon emission amount, improving the topsoil produced because burning straw has great environmental benefit, economic benefit and social benefit.
Biomass anaerobic low-temperature pyrolysis product has 4 kinds: a. gas-phase product, with methane be major ingredient high heating value biological mass combustable gas; B. liquid product wood tar oil; C. liquid product wood vinegar; D. solid product biomass charcoal.) all there is Jie Neng Minus row and very high economic worth.
Current biomass low-temperature pyrolysis technique combustion gas is plunged to about 80 ~ 100 DEG C, and lower than the boiling point of wood tar oil and wood vinegar, these two kinds of material post liquefaction are separated out from gas phase simultaneously, produces the mixture of wood tar oil and wood vinegar.After this this mixture is stored in closed hollow place and continues half a year more than, be separated by the proportion difference of two kinds of materials.This Measures compare is original, and floor space is large, also reduces the quality of wood tar oil and wood vinegar simultaneously, is not suitable for modernization and large-scale production, must be improved.
Utility model content
The purpose of this utility model is to provide a kind of fast wind cold mould biomass anaerobic low-temperature pyrolysis product separation system.
The purpose of this utility model is achieved through the following technical solutions:
A kind of fast wind cold mould biomass anaerobic low-temperature pyrolysis product separation system, comprise gas retort, the air outlet of described gas retort connects force one wind water cooler by pipeline, the air outlet of described force one wind water cooler connects the first gas-liquid separator, the bottom end outlet connected wood tar container for storing liquid of described first gas-liquid separator, the outlet side of described first gas-liquid separator connects two-stage water-cooling but device, the outlet side of described two-stage water-cooling but device connects the second gas-liquid separator, the bottom end outlet of described first gas-liquid separator connects wood vinegar container for storing liquid, the outlet side of described second gas-liquid separator connects absorbent charcoal adsorption tank, the outlet side of described absorbent charcoal adsorption tank connects the second roots blower, described second roots blower connects gas storage tank.
Further, described force one wind water cooler comprises the first cast housing, the import of described first cast housing is connected with described gas retort, the outlet of described first cast housing is connected with the first gas-liquid separator, described first cast housing internal jacket is provided with multiple forced air cooled tube, the two ends of described forced air cooled tube are all fixedly connected with the first roots blower through described first cast housing, form air-cooled loop.
Further, described two-stage water-cooling but device comprises the second cast housing, the import of described second cast housing is fixedly connected with cold water source, the outlet of described second cast housing is fixedly connected with water shoot, described second cast housing internal jacket is provided with pneumatic tube, the inlet end of described pneumatic tube passes the second cast housing and is communicated with the outlet side of the first gas-liquid separator, and the outlet side of described pneumatic tube is passed the second cast housing and is communicated with the inlet end of the second gas-liquid separator.
Further, the height of the inlet mouth present position of described first gas-liquid separator, lower than the height of its present position, air outlet, increases the path of mixed gas in the first gas-liquid separator, thus increases separating effect.
Further, the height of the inlet mouth present position of described second gas-liquid separator, lower than the height of its present position, air outlet, increases the path of mixed gas in the second gas-liquid separator, thus increases separating effect.。
Further, the bottom of described absorbent charcoal adsorption tank and top are respectively equipped with inlet mouth and air outlet, are provided with some horizontally disposed activated carbon filter layers in described absorbent charcoal adsorption tank.
Further, liquid level indicator is equipped with in described one-level gas-liquid separator and secondary gas-liquid separator.
The beneficial effects of the utility model are: the utility model is cooled and the second-order separation by secondary, realize being rapidly and efficiently separated wood tar oil and wood vinegar, by acid aerosol remaining in the adsorbed gas of property charcoal adsorption tanks, purification mixed gas, obtains the inflammable mixture of high purity; Native system meets the Production requirement of modernization, mass-producing, serialization, whole system compact construction, and floor space is little, and cost is low.
Accompanying drawing explanation
With reference to the accompanying drawings the utility model is described in further detail below.
Fig. 1 is the structural representation of fast wind cold mould biomass anaerobic low-temperature pyrolysis product separation system described in the utility model embodiment.
In figure:
1, gas retort; 2, the first cast housing; 3, forced air cooled tube; 4, the first roots blower; 5, the first gas-liquid separator; 6, wood tar oil container for storing liquid; 7, the second cast housing; 8, cold water source; 9, water shoot; 10, the second gas-liquid separator; 11, wood vinegar container for storing liquid; 12, absorbent charcoal adsorption tank; 13, the second roots blower; 14, gas storage tank; 15, pneumatic tube.
Embodiment
As shown in Figure 1, a kind of fast wind cold mould biomass anaerobic low-temperature pyrolysis product separation system described in the utility model embodiment, comprise gas retort 1, the air outlet of described gas retort 1 connects force one wind water cooler by pipeline, the gas phase mixture of gas retort 1 output is through force one wind water cooler fast cooling, described force one wind water cooler comprises the first cast housing 2, the import of described first cast housing 2 is connected with the air outlet of gas retort 1, the outlet of described first cast housing 2 is connected with the first gas-liquid separator 5, described first cast housing 2 internal jacket is provided with multiple forced air cooled tube 3, the two ends of described forced air cooled tube 3 are all fixedly connected with the first roots blower 4 through described first cast housing 2, form air-cooled loop, for the mixed gas cooling outside forced air cooled tube 3.
Mixed gas through the cooling of force one wind water cooler enters into the laggard row gas-liquid separation of the first gas-liquid separator 5, the bottom that isolated wood tar oil flows to the first gas-liquid separator 5 is converged, flow in connected wood tar oil container for storing liquid 6 from the bottom end outlet of the first gas-liquid separator 5 and store, achieve and isolate wood tar oil from mixed gas.
The outlet side of described first gas-liquid separator 5 connects two-stage water-cooling but device, from the first gas-liquid separator 5 mixed gas out enter into two-stage water-cooling but device cool further, described two-stage water-cooling but device comprises the second cast housing 7, the import of described second cast housing 7 is fixedly connected with cold water source 8, the outlet of described second cast housing 7 is fixedly connected with water shoot 9, form Water-cooling circulating, described second cast housing 7 internal jacket is provided with pneumatic tube 15, the inlet end of described pneumatic tube 15 passes the second cast housing 7 and is communicated with the outlet side of the first gas-liquid separator 5, the outlet side of described pneumatic tube 15 is passed the second cast housing 7 and is communicated with the inlet end of the second gas-liquid separator 10, realize cold water cooling, cold water and mixed gas are separated simultaneously.
The mixed gas flowed out from the outlet side of described two-stage water-cooling but device enters into the second gas-liquid separator 10 and carries out gas-liquid separation, the bottom end outlet of described first gas-liquid separator 5 connects wood vinegar container for storing liquid 11, the bottom that isolated wood vinegar flows to the second gas-liquid separator 10 is converged, flow in connected wood vinegar container for storing liquid 11 from the bottom end outlet of the second gas-liquid separator 10 and store, achieve and isolate wood vinegar from mixed gas.
The outlet side of described second gas-liquid separator 10 connects absorbent charcoal adsorption tank 12, bottom and the top of described absorbent charcoal adsorption tank 12 are respectively equipped with inlet mouth and air outlet, some horizontally disposed activated carbon filter layers are provided with in described absorbent charcoal adsorption tank 12, the adsorptive of described absorbent charcoal adsorption tank 12 is the self-produced gac of gas retort 1, realize gas retort 1 its lytic activity charcoal self-produced personal, higher economic benefit can be obtained, mixed gas adsorbs the acid aerosol of trace through absorbent charcoal adsorption tank 12, further purification gas mixture, obtain the inflammable mixture of high heating value, the outlet side of described absorbent charcoal adsorption tank 12 connects the second roots blower 13, second roots blower 13 provides power for whole system, described second roots blower 13 connects gas storage tank 14, the pure inflammable gas filtered from absorbent charcoal adsorption tank 12 enters into storage in gas storage tank 14.
The utility model is not limited to above-mentioned preferred forms; anyone can draw other various forms of products under enlightenment of the present utility model; no matter but any change is done in its shape or structure; every have identical with the application or akin technical scheme, all drops within protection domain of the present utility model.
Claims (7)
1. a fast wind cold mould biomass anaerobic low-temperature pyrolysis product separation system, comprise gas retort, it is characterized in that: the air outlet of described gas retort connects force one wind water cooler by pipeline, the air outlet of described force one wind water cooler connects the first gas-liquid separator, the bottom end outlet connected wood tar container for storing liquid of described first gas-liquid separator, the outlet side of described first gas-liquid separator connects two-stage water-cooling but device, the outlet side of described two-stage water-cooling but device connects the second gas-liquid separator, the bottom end outlet of described first gas-liquid separator connects wood vinegar container for storing liquid, the outlet side of described second gas-liquid separator connects absorbent charcoal adsorption tank, the outlet side of described absorbent charcoal adsorption tank connects roots blower, described roots blower connects gas storage tank.
2. separation system according to claim 1, it is characterized in that: described force one wind water cooler comprises the first cast housing, the import of described first cast housing is connected with described gas retort, the outlet of described first cast housing is connected with the first gas-liquid separator, described first cast housing internal jacket is provided with multiple forced air cooled tube, the two ends of described forced air cooled tube are all fixedly connected with the first roots blower through described first cast housing, form air-cooled loop.
3. separation system according to claim 1, it is characterized in that: described two-stage water-cooling but device comprises the second cast housing, the import of described second cast housing is fixedly connected with cold water source, the outlet of described second cast housing is fixedly connected with water shoot, described second cast housing internal jacket is provided with pneumatic tube, the inlet end of described pneumatic tube passes the second cast housing and is communicated with the outlet side of the first gas-liquid separator, and the outlet side of described pneumatic tube is passed the second cast housing and is communicated with the inlet end of the second gas-liquid separator.
4. separation system according to claim 1, is characterized in that: the height of the inlet mouth present position of described first gas-liquid separator is lower than the height of its present position, air outlet.
5. separation system according to claim 1, is characterized in that: the height of the inlet mouth present position of described second gas-liquid separator is lower than the height of its present position, air outlet.
6. separation system according to claim 1, is characterized in that: the bottom of described absorbent charcoal adsorption tank and top are respectively equipped with inlet mouth and air outlet, is provided with some horizontally disposed activated carbon filter layers in described absorbent charcoal adsorption tank.
7. separation system according to claim 1, is characterized in that: be equipped with liquid level indicator in described one-level gas-liquid separator and secondary gas-liquid separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520124243.6U CN204981748U (en) | 2015-03-04 | 2015-03-04 | Quick air -cooled type living beings anaerobic low temperature pyrolysis result piece -rate system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520124243.6U CN204981748U (en) | 2015-03-04 | 2015-03-04 | Quick air -cooled type living beings anaerobic low temperature pyrolysis result piece -rate system |
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| Publication Number | Publication Date |
|---|---|
| CN204981748U true CN204981748U (en) | 2016-01-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520124243.6U Expired - Fee Related CN204981748U (en) | 2015-03-04 | 2015-03-04 | Quick air -cooled type living beings anaerobic low temperature pyrolysis result piece -rate system |
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| CN (1) | CN204981748U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701213A (en) * | 2016-12-09 | 2017-05-24 | 广西北海浩邦新能源科技有限公司 | Gas purifying and flue gas recycling method |
| CN110229683A (en) * | 2019-04-01 | 2019-09-13 | 谷峻峰 | A kind of carbonization production wood vinegar biological flue gas system |
-
2015
- 2015-03-04 CN CN201520124243.6U patent/CN204981748U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701213A (en) * | 2016-12-09 | 2017-05-24 | 广西北海浩邦新能源科技有限公司 | Gas purifying and flue gas recycling method |
| CN110229683A (en) * | 2019-04-01 | 2019-09-13 | 谷峻峰 | A kind of carbonization production wood vinegar biological flue gas system |
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| 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: 20160120 Termination date: 20170304 |
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| CF01 | Termination of patent right due to non-payment of annual fee |