CN110373216A - A kind of gas-liquid separator and apparatus for thermal cleavage - Google Patents
A kind of gas-liquid separator and apparatus for thermal cleavage Download PDFInfo
- Publication number
- CN110373216A CN110373216A CN201910640836.0A CN201910640836A CN110373216A CN 110373216 A CN110373216 A CN 110373216A CN 201910640836 A CN201910640836 A CN 201910640836A CN 110373216 A CN110373216 A CN 110373216A
- Authority
- CN
- China
- Prior art keywords
- liquid
- pipeline
- gas
- wood vinegar
- fuel gas
- 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.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 74
- 238000003776 cleavage reaction Methods 0.000 title claims description 10
- 230000007017 scission Effects 0.000 title claims description 10
- 235000021419 vinegar Nutrition 0.000 claims abstract description 28
- 239000000052 vinegar Substances 0.000 claims abstract description 28
- 239000002023 wood Substances 0.000 claims abstract description 28
- 238000000605 extraction Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 2
- 239000002737 fuel gas Substances 0.000 abstract description 28
- 239000007789 gas Substances 0.000 abstract description 23
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 14
- 229910052799 carbon Inorganic materials 0.000 abstract description 13
- 239000002253 acid Substances 0.000 abstract description 12
- 239000000428 dust Substances 0.000 abstract description 10
- 239000010419 fine particle Substances 0.000 abstract description 10
- 238000004227 thermal cracking Methods 0.000 abstract description 6
- 239000002028 Biomass Substances 0.000 description 5
- 239000000567 combustion gas Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- 239000012075 bio-oil Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000000366 juvenile effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C5/00—Production of pyroligneous acid distillation of wood, dry distillation of organic waste
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Gas Separation By Absorption (AREA)
Abstract
One embodiment of the present invention discloses a kind of gas-liquid separator, it include: U-shaped pipeline, pipeline one end is provided with air inlet, and the other end of pipeline is provided with gas outlet, the bottom of pipeline is provided with a switch valve, and the liquid that density is lower than wood vinegar and wood vinegar of getting along well dissolves each other is filled in pipeline.The fuel gas obtained after thermal cracking is complete enters in pipeline from air inlet, and the air pressure at air inlet is higher than the air pressure of gas outlet, and fuel gas is forced through the liquid in pipeline and reaches at gas outlet；During fuel gas passes through liquid, fine particle carbon dust is by liquid acquisition, gaseous acid reacts the wood vinegar for being reduced into liquid with liquid chilling, wood vinegar density relative liquid is higher, after obstructed liquid is stood in pipeline, wood vinegar fall to liquid bottom and and liquid layered, wood vinegar is discharged by unlatching switch valve at this time, above-mentioned technical proposal can be convenient efficiently by fuel gas fine particle carbon dust and gaseous acid remove, clever structure.
Description
Technical field
The present invention relates to technical field of waste treatment, in particular to a kind of gas-liquid separator and apparatus for thermal cleavage.
Background technique
Biomass energy is a kind of green, clean energy resource, and is a kind of unique renewable carbon source, and Biomass-pyrolysis is
The important form of biomass utilization, it can make biomass energy be converted to other energy forms such as bio oil, it is easily stored and
It uses.With the appearance of oil crisis and the development and utilization of new energy technology, Biomass-pyrolysis more and more attention has been paid to.
Bio oil, fuel gas and biomass carbon can be generated during existing biomass through pyrolysis, what is obtained after thermal cracking is complete can
Contain fine particle carbon dust and gaseous acid in combustion gas body, the existing separator structure for removing impurity in fuel gas is multiple
It is miscellaneous, it is with high costs, a kind of structure, which is provided, for the invention is simply to auxiliary isolation of purified gas-liquid separator and apparatus for thermal cleavage.
Summary of the invention
It is an object of the invention at least solve one of the technical problems existing in the prior art, a kind of gas-liquid separation is provided
Device and apparatus for thermal cleavage can cleverly remove fine particle carbon dust and gaseous acid in fuel gas simultaneously.
According to the first aspect of the invention, a kind of gas-liquid separator is provided, comprising: U-shaped pipeline, described pipeline one end
It is provided with air inlet, the other end of the pipeline is provided with gas outlet, and the bottom of the pipeline is provided with a switch valve, the pipe
It is lower than the liquid that wood vinegar and discord wood vinegar dissolve each other filled with density in road.
The gas outlet is connected with an air extraction compressor.
The end that the pipeline is provided with the gas outlet is higher than the end for being provided with the air inlet.
The liquid is set as pure water.
The both ends of the pipeline all have opening, and the opening is provided with first flange, and the opening is close by covering
Envelope, it is described capping with the opening junction be provided with second flange, be provided in the capping air inlet or it is described out
Port.
Any of the above-described technical solution at least has a following advantageous effects: the fuel gas obtained after thermal cracking is complete from
Air inlet enters in pipeline, and during fuel gas is constantly accumulated, the air pressure at air inlet is higher than the gas of gas outlet
Pressure, fuel gas are forced through the liquid in pipeline and reach at gas outlet；During fuel gas passes through liquid, subtle
For grain carbon dust by liquid acquisition, gaseous acid reacts the wood vinegar for being reduced into liquid with liquid chilling, wood vinegar density relative liquid compared with
Height, after obstructed liquid is stood in pipeline, wood vinegar fall to liquid bottom and and liquid layered, at this time by opening switch
Wood vinegar is discharged valve, it is seen that above-mentioned technical proposal can be convenient the fine particle carbon dust and gaseous state in fuel gas efficiently
Acid removal, simple and ingenious structure.
A kind of apparatus for thermal cleavage, including a kind of gas-liquid separator.
Above-mentioned technical proposal at least has a following advantageous effects: the fuel gas obtained after thermal cracking is complete is from air inlet
Mouth enters in pipeline, and during fuel gas is constantly accumulated, the air pressure at air inlet is higher than the air pressure of gas outlet, can
Combustion gas body is forced through the liquid in pipeline and reaches at gas outlet；During fuel gas passes through liquid, fine particle carbon
Powder is by liquid acquisition, and gaseous acid reacts the wood vinegar for being reduced into liquid with liquid chilling, and wood vinegar density relative liquid is higher,
After obstructed liquid is stood in pipeline, wood vinegar fall to liquid bottom and and liquid layered, at this time will by opening switch valve
Wood vinegar discharge, it is seen that the apparatus for thermal cleavage of above-mentioned technical proposal can be convenient the fine particle carbon in fuel gas efficiently
Powder and gaseous acid removal, simple and ingenious structure.
Detailed description of the invention
The present invention is further explained with reference to the accompanying drawings and examples；
Fig. 1 is the schematic diagram of one embodiment of the present invention.
Specific embodiment
This part will be described in specific embodiments of the present invention, and the preferred embodiments of the invention is shown in the accompanying drawings, attached
The effect of figure be with figure remark additionally book word segment description, enable a person to intuitively, visually understand of the invention
Each technical characteristic and overall technical architecture, but it should not be understood as limiting the scope of the invention.
In the description of the present invention, it is to be understood that, be related to orientation description, for example, above and below, front, rear, left and right etc.
The orientation or positional relationship of instruction is to be based on the orientation or positional relationship shown in the drawings, and is merely for convenience of the description present invention and letter
Change description, rather than the device or element of indication or suggestion meaning must have a particular orientation, with specific orientation construct and
Operation, therefore be not considered as limiting the invention.
In the description of the present invention, several to be meant that one or more, it is multiple to be meant that two or more, be greater than,
Be less than, more than etc. be interpreted as not including this number, it is above, following, within etc. be interpreted as including this number.If there is being described to first,
Second is only intended to for the purpose of distinguishing technical characteristic, is not understood to indicate or imply relative importance or implicitly indicates institute
The quantity of the technical characteristic of instruction or the precedence relationship for implicitly indicating indicated technical characteristic.
In description of the invention, unless otherwise restricted clearly, the words such as setting, installation, connection be shall be understood in a broad sense, institute
Above-mentioned word in the present invention specific can rationally be determined with the particular content of combination technology scheme by belonging to technical field technical staff
Meaning.
Referring to Fig.1, a kind of gas-liquid separator, comprising: U-shaped pipeline 1,1 one end of pipeline are provided with air inlet 2, pipeline 1
The other end be provided with gas outlet 3, the bottom of pipeline 1 is provided with a switch valve 4, is lower than wood vinegar 5 filled with density in pipeline 1
And the liquid 6 that wood vinegar 5 of getting along well dissolves each other, liquid 6 is preferably arranged to pure water, is easily obtained, low in cost.After thermal cracking is complete
Obtained fuel gas enters in pipeline 1 from air inlet 2, gas during fuel gas is constantly accumulated, at air inlet 2
Pressure is higher than the air pressure of gas outlet 3, and fuel gas is forced through the liquid 6 in pipeline 1 and reaches at gas outlet 3；In fuel gas
During liquid 6, fine particle carbon dust is intercepted by liquid 6, and gaseous acid reacts the wood for being reduced into liquid with 6 chilling of liquid
Vinegar liquid 5,5 density relative liquid 6 of wood vinegar is higher, and after obstructed liquid 6 is stood in pipeline 1, wood vinegar 5 falls to liquid 6
Bottom is simultaneously layered with liquid 6, wood vinegar 5 is discharged by opening switch valve 4 at this time, it is seen that above-mentioned technical proposal can be convenient fastly
Prompt fine particle carbon dust and gaseous acid by fuel gas removes, simple and ingenious structure.
As shown in Figure 1, in some embodiments, in order to accelerate fuel gas by liquid 6, being connected in gas outlet 3
One air extraction compressor reduces the air pressure near gas outlet 3 by air extraction compressor, improves gas outlet 3 nearby and near air inlet 2
Pressure difference so that fuel gas is more easier across liquid 6.
When fuel gas passes through liquid 6, the liquid level of the opposite air inlet 2 of liquid level meeting near gas outlet 3 is higher, excellent thus
Choosing, the end that pipeline 1 is provided with gas outlet 3 is higher than the end for being provided with air inlet 2, can save 1 consumptive material of pipeline, subtract simultaneously
Education and correction for juvenile offenders road 1 is taken up space.
As shown in Figure 1, in some embodiments, the both ends of pipeline 1 all have opening, opening is provided with first flange
8, opening is provided with second flange 9 with opening junction by 7 sealing of capping, capping 7, and air inlet 2 is provided in capping 7 or is gone out
It is solid by bolt to be provided with sealing rubber ring, first flange 8 and second flange 9 for port 3 between first flange 8 and second flange 9
It is fixed, by the removably sealed opening of capping 7, convenient for the later period to carrying out clean and maintenance in pipeline 1.
A kind of apparatus for thermal cleavage, including a kind of gas-liquid separator.Obtained fuel gas is from air inlet after thermal cracking is complete
Mouth 2 enters in pipeline 1, and during fuel gas is constantly accumulated, the air pressure at air inlet 2 is higher than the gas of gas outlet 3
Pressure, fuel gas are forced through the liquid 6 in pipeline 1 and reach at gas outlet 3；During fuel gas passes through liquid 6, carefully
Microparticle carbon dust is intercepted by liquid 6, and gaseous acid reacts the wood vinegar 5 for being reduced into liquid, 5 density phase of wood vinegar with 6 chilling of liquid
Higher to liquid 6, after obstructed liquid 6 is stood in pipeline 1, wood vinegar 5 falls to 6 bottom of liquid and is layered with liquid 6, this
When by open switch valve 4 wood vinegar 5 is discharged, it is seen that the apparatus for thermal cleavage of above-mentioned technical proposal, which can be convenient, efficiently may be used
Fine particle carbon dust and gaseous acid removal in combustion gas body, simple and ingenious structure.
The embodiment of the present invention is explained in detail above in conjunction with attached drawing, but the present invention is not limited to the above embodiments,
The technical field those of ordinary skill within the scope of knowledge, can also make without departing from the purpose of the present invention
Various change out.
Claims (6)
1. a kind of gas-liquid separator characterized by comprising U-shaped pipeline, described pipeline one end are provided with air inlet, institute
The other end for stating pipeline is provided with gas outlet, and the bottom of the pipeline is provided with a switch valve, is filled with density in the pipeline
Lower than wood vinegar and the liquid that dissolves each other of wood vinegar of getting along well.
2. a kind of gas-liquid separator as described in claim 1, it is characterised in that the gas outlet is connected with an air extraction compressor.
3. a kind of gas-liquid separator as described in claim 1, it is characterised in that the pipeline is provided with the end of the gas outlet
Portion is higher than the end for being provided with the air inlet.
4. a kind of gas-liquid separator as described in claim 1, it is characterised in that the liquid is set as pure water.
5. a kind of gas-liquid separator as described in claim 1, it is characterised in that the both ends of the pipeline all have opening, described
Opening is provided with first flange, and the opening is provided with second with the opening junction by lidstock, the capping
Flange is provided with the air inlet or the gas outlet in the capping.
6. a kind of apparatus for thermal cleavage, it is characterised in that including a kind of gas-liquid separator a method as claimed in any one of claims 1 to 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910640836.0A CN110373216A (en) | 2019-07-16 | 2019-07-16 | A kind of gas-liquid separator and apparatus for thermal cleavage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910640836.0A CN110373216A (en) | 2019-07-16 | 2019-07-16 | A kind of gas-liquid separator and apparatus for thermal cleavage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110373216A true CN110373216A (en) | 2019-10-25 |
Family
ID=68253432
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910640836.0A Pending CN110373216A (en) | 2019-07-16 | 2019-07-16 | A kind of gas-liquid separator and apparatus for thermal cleavage |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110373216A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114558351A (en) * | 2022-03-29 | 2022-05-31 | 绍兴市三合检测技术有限公司 | Oil-liquid separator |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06228577A (en) * | 1993-02-01 | 1994-08-16 | Shin Meiwa Ind Co Ltd | Carbonization equipment |
| CN203648335U (en) * | 2014-01-03 | 2014-06-18 | 王兴德 | Smoke-abatement, dust-removal and sulfur-removal vapor-pressure type water circulation system for boiler |
| CN105219447A (en) * | 2015-09-24 | 2016-01-06 | 湖南省金本低碳科技有限公司 | The separating of oil purification-recovery system of a kind of biomass gas-liquid |
| CN108728165A (en) * | 2018-08-16 | 2018-11-02 | 福建中化智胜化肥有限公司 | Charcoal base manure resources of production method of comprehensive utilization based on updraft type charcoal gas coproduction stove |
| CN109794120A (en) * | 2019-03-25 | 2019-05-24 | 广东洁冠能源科技有限公司 | Bubble deduster and its application method |
| CN210394267U (en) * | 2019-07-16 | 2020-04-24 | 中山市至善生物科技有限公司 | Gas-liquid separator and thermal cracking equipment |
-
2019
- 2019-07-16 CN CN201910640836.0A patent/CN110373216A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06228577A (en) * | 1993-02-01 | 1994-08-16 | Shin Meiwa Ind Co Ltd | Carbonization equipment |
| CN203648335U (en) * | 2014-01-03 | 2014-06-18 | 王兴德 | Smoke-abatement, dust-removal and sulfur-removal vapor-pressure type water circulation system for boiler |
| CN105219447A (en) * | 2015-09-24 | 2016-01-06 | 湖南省金本低碳科技有限公司 | The separating of oil purification-recovery system of a kind of biomass gas-liquid |
| CN108728165A (en) * | 2018-08-16 | 2018-11-02 | 福建中化智胜化肥有限公司 | Charcoal base manure resources of production method of comprehensive utilization based on updraft type charcoal gas coproduction stove |
| CN109794120A (en) * | 2019-03-25 | 2019-05-24 | 广东洁冠能源科技有限公司 | Bubble deduster and its application method |
| CN210394267U (en) * | 2019-07-16 | 2020-04-24 | 中山市至善生物科技有限公司 | Gas-liquid separator and thermal cracking equipment |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114558351A (en) * | 2022-03-29 | 2022-05-31 | 绍兴市三合检测技术有限公司 | Oil-liquid separator |
| CN114558351B (en) * | 2022-03-29 | 2023-08-22 | 绍兴市三合检测技术有限公司 | Oil-liquid separator |
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| TA01 | Transfer of patent application right |
Effective date of registration: 20230111 Address after: Room 420-2, 4th Floor, Hongbaolong Hotel, West Tower, Tangsheng International Business Center B, No. 1-2, Chengnan 1st Road, South District, Zhongshan City, Guangdong Province, 528400 Applicant after: Guangdong YouCarbon Technology Co.,Ltd. Address before: Room 210, Building 2, No. 28, Yanjiang East Road, Torch Development Zone, Zhongshan City, Guangdong Province, 528400 Applicant before: ZHONGSHAN ZHISHAN BIOTECHNOLOGY Co.,Ltd. |
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