CN202039029U - Tar wood vinegar separator - Google Patents

Tar wood vinegar separator Download PDF

Info

Publication number
CN202039029U
CN202039029U CN2011201580701U CN201120158070U CN202039029U CN 202039029 U CN202039029 U CN 202039029U CN 2011201580701 U CN2011201580701 U CN 2011201580701U CN 201120158070 U CN201120158070 U CN 201120158070U CN 202039029 U CN202039029 U CN 202039029U
Authority
CN
China
Prior art keywords
tar
separator
wood vinegar
separator tank
delivery line
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
Application number
CN2011201580701U
Other languages
Chinese (zh)
Inventor
熊建
何涛
周碧涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
WUHAN TIANYING ENVIRONMENTAL ENGINEERING Co Ltd
Original Assignee
WUHAN TIANYING ENVIRONMENTAL ENGINEERING Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by WUHAN TIANYING ENVIRONMENTAL ENGINEERING Co Ltd filed Critical WUHAN TIANYING ENVIRONMENTAL ENGINEERING Co Ltd
Priority to CN2011201580701U priority Critical patent/CN202039029U/en
Application granted granted Critical
Publication of CN202039029U publication Critical patent/CN202039029U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Abstract

The utility model relates to a tar wood vinegar separator which comprises a box body with one horizontal bottom surface. An inner cavity of the tar wood vinegar separator is divided into two cavities of a first separation tank (1) and a second separation tank (2) by a partition plate (5); the upper part of the first separation tank (1) is communicated with a liquid inlet pipe (3), an opening is arranged at the bottom part of the first separation tank (1), and the bottom part is communicated wiht a tar guide-out pipe (8). The upper part of the second separation tank (2) is communicated wiht a wood vinegar guide-out pipe (9), an opening is arranged at the bottom part, and the bottom part is communicated with the tar guide-out pipe (8). As the two separation tanks of the tar wood vinegar separator are formed by dividing one box body through the partition plate, the tar wood vinegar separator has low material consumption and low manufacturing cost, and the openings at the bottom parts of the two separation tanks are positioned on the same height; and when valves are simultaneoulsy opened to guide out the tar, the tar backflow phenomenon can be avoided and good liquid separation effect is achieved.

Description

A kind of tar wood vinegar separator
Technical field
The utility model relates to a kind of tar wood vinegar separator, and particularly a kind of tar wood vinegar separator that is used for the marsh gas purifying device belongs to gasifying biomass and separation technology field.
Background technology
The renewable energy source that biogas is a kind of cleaning, convenience, thermal efficiency is high; it is a kind of inflammable gas that is generated by the microbiological degradation fermentation at anaerobic condition by organism such as agricultural crop straw, forest tree castoff, sawdust, edible fungi residues, cattle and sheep animal manures; can replace fuel such as the traditional straw that uses in Rural areas, firewood; reduce environmental pollution, protection health of people; and reduce overcut to environment damage, safeguard good ecology.But the complicated component of biogas contains a large amount of gases and liquid impurity, influences the use of biogas, therefore needs before use biogas to be carried out purifying treatment.
Liquid impurity in the biogas is mainly the mixed solution of tar and wood vinegar.Tar viscosity is very strong, attached to stopping up gas passage on the tube wall easily, makes biogas interrupt and the flame-out phenomenon of generation.Wood vinegar is a kind of incombustible liquid, and its reduces the burning usefulness of biogas and influences the use of biogas.But then, wood vinegar is a kind of material of purposes widely that has, can be used for soil improvement, deodorizing, plant-growth regulator, preservation food, fodder additives etc., also a kind of very important organism of tar, therefrom multiple industrial chemicals be can extract, plastics, synthon, dyestuff, rubber, medicine, high temperature material are used to produce.Therefore, in to marsh gas purifying, separating tar and wood vinegar mixing liquid, also need further tar to be separated with wood vinegar, so that further recycle.
Referring to Fig. 1, tar wood vinegar separator in the existing marsh gas purifying device, form by two separated grooves, comprise first separator tank 1 and second separator tank 2, liquid-inlet pipe 3 is arranged on the top of first separator tank 1, and wherein, the top of first separator tank 1 and bottom are higher than second separator tank 2, first separator tank, 1 top is higher than connecting tube 4 on the outer side wall of second separator tank 2, and the other end of conduit 4 is communicated with second separator tank 2.The bottom of first separator tank 1 and second separator tank 2 is respectively equipped with the pipeline that is connected with same tar delivery line 8, is connected with the first separator tank valve 6 and the second separator tank valve 7 on the pipeline between first separator tank 1 and second separator tank 2 and the tar delivery line 8 respectively.The tar of separating through refining plant and the mixing liquid of wood vinegar at first enter first separator tank 1 and precipitate, tar density is deposited on bottom land greatly, the density of wood vinegar is less and above floating over, top wood vinegar enters second separator tank 2 by conduit 4 and precipitates.After precipitation was finished, wood vinegar was derived through the take-up gear on second separator tank, 2 tops, and the tar delivery line 8 that tar is connected through two separator tank bottoms is derived, and realizes separating of tar and wood vinegar.
But there is following defective in the tar wood vinegar separator in the existing marsh gas purifying device: the first, two separator tank independently is provided with, and it is more to make material requested, and cost is higher; Second, because the bottom of two separator tanks is not at sustained height, the potential energy of first separator tank, the 1 interior tar that the bottom is higher is higher, when open the first separator tank valve 6 and the second separator tank valve 7 simultaneously, when from first separator tank 1 and second separator tank 2, deriving tar, can produce the tar backflow phenomenon, promptly can pass through the first separator tank valve 6, tar delivery line 8 and the second separator tank valve 7 mobile to second separator tank 2 in for the tar in first separator tank 1, influences the separating effect and the quality of second separator tank, 2 interior wood vinegar; Liquid level in the three, the second separator tank 2 is higher, and the jacking of the tar that is subjected to refluxing also can cause the wood vinegar in second separator tank 2 to overflow from the cell body upper edge, causes the waste of wood vinegar and to the pollution of environment.
Summary of the invention
The purpose of this utility model is that the separator tank that overcomes the tar wood vinegar separator existence in the existing marsh gas purifying device independently is provided with, the manufacturing cost height, and easily produce the tar backflow phenomenon when discharging tar simultaneously, influence separating effect, and the tar backflow causes the excessive shortcomings and deficiencies of wood vinegar, provide a kind of two separator tanks to merge setting, low cost of manufacture, and can reduce the influence of tar backflow effect, avoid occurring the tar wood vinegar separator of the excessive phenomenon of wood vinegar the liquid separation effect.
The utility model for realizing the technical scheme that technical purpose adopts is:
A kind of tar wood vinegar separator, described separator comprises the casing of a bottom surface level, described casing internal fixing has dividing plate, the top margin of described dividing plate is lower than the end face of casing, described dividing plate is divided into disconnected first separator tank and two inner chambers of second separator tank with casing, described separator also comprises liquid-inlet pipe, tar delivery line and wood vinegar delivery line, the top of described first separator tank is communicated with liquid-inlet pipe, the bottom is provided with the pipeline that is connected with the tar delivery line, be connected the first separator tank valve on the pipeline between first separator tank and the tar delivery line, the top of described second separator tank is communicated with the wood vinegar delivery line, the bottom is provided with the pipeline that is connected with the tar delivery line, is connected with the second separator tank valve on the pipeline between second separator tank and the tar delivery line.
A kind of tar wood vinegar separator, the casing of described separator is a rectangular parallelepiped.
A kind of tar wood vinegar separator, the volume of described first separator tank and second separator tank equates.
A kind of tar wood vinegar separator, the height of described dividing plate is 70%~90% of a box height.
Compared with prior art, characteristics of the present utility model are:
1. two separator tanks adopt a casing and separate setting with dividing plate and form few, the low cost of manufacture of materials used.
2. two separator tanks are positioned at sustained height with the opening that the tar delivery line is connected, and when opening valve derivation tar simultaneously, can reduce impact and the mixing of tar backflow effect to liquid in second separator tank, and liquid separation is effective.
3. the wood vinegar liquid level in second separator tank is lower, is subjected to tar and refluxes and to do the time spent, wood vinegar can not occur from the excessive phenomenon in cell body upper edge, avoids waste and pollutes.
Description of drawings
Fig. 1 is the structural representation of existing tar wood vinegar separator.
Fig. 2 is the structural representation of tar wood vinegar separator of the present utility model.
Among the figure: first separator tank, 1, the second separator tank 2, liquid-inlet pipe 3, conduit 4, dividing plate 5, the first separator tank valves 6, the second separator tank valves 7, tar delivery line 8, wood vinegar delivery line 9.
Embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described further.
As shown in Figure 2, tar wood vinegar separator of the present utility model, agent structure is the casing of a bottom surface level, and the casing internal fixing has dividing plate 5, and dividing plate 5 is divided into two inner chambers that are not connected with casing, respectively as first separator tank 1 and second separator tank 2.Make and use for convenient, casing can be made rectangular shape.First separator tank 1 is coal-tar middle oil with mixing liquid relevant with ratio wood vinegar with the volumetrical setting of second separator tank 2, and generalized case can be set to identical volume by two separator tanks.The top margin of dividing plate 5 is lower than the end face of casing, that is to say the height of the height of dividing plate 5 less than casing, so that liquid is from first separator tank, 1 overflow to the second separator tank 2.The height of dividing plate 5 can be set to 70%~90% of box height.The top of first separator tank 1 is communicated with liquid-inlet pipe 3, and the bottom is provided with the pipeline that is connected with tar delivery line 8, also is connected with the first separator tank valve 6 on the pipeline between first separator tank 1 and the tar delivery line 8.The top of second separator tank 2 is communicated with wood vinegar delivery line 9, and the bottom is provided with the pipeline that is connected with tar delivery line 8, is connected with the second separator tank valve 7 on the pipeline between second separator tank 2 and the tar delivery line 8.
At first entering first separator tank from the mixing liquid of isolated tar of marsh gas purifying device and wood vinegar from liquid-inlet pipe 3 precipitates, tar density is deposited on bottom land greatly, wood vinegar density is less and float over top, because the top margin of dividing plate 5 is lower than the end face of casing, the wood vinegar on the first separator tank top is spilled over to second separator tank 2 from dividing plate 5 tops.The liquid that enters second separator tank 2 precipitates again, makes tar deposition in the bottom, and wood vinegar floats over top.After precipitation was finished, the vinegar liquid pool is derived and entered to the wood vinegar on second separator tank, 2 tops through take-up gear, and the tar of two separator tank bottoms is derived by tar delivery line 8 and entered tar pool, thereby finish separating and reclaiming of tar and wood vinegar.The derivation of tar can be controlled by the first separator tank valve 6 and the second separator tank valve 7, opens the first separator tank valve 6 and the second separator tank valve 7 usually simultaneously, and the interior sedimentary tar of two separator tanks is derived simultaneously.
Two separator tanks of the tar wood vinegar separator that the utility model provides adopt a casing to separate to be provided with dividing plate and form, few, the low cost of manufacture of materials used, and two separator tanks are positioned at sustained height with the opening that the tar delivery line is connected, when opening valve derivation tar simultaneously, when opening valve derivation tar simultaneously, can reduce impact and the mixing of tar backflow effect to liquid in second separator tank, liquid separation is effective.The box body wall of the second separator tank periphery is higher, and wood vinegar liquid level wherein is relatively low, is subjected to tar and refluxes and to do the time spent, wood vinegar can not occur from the excessive phenomenon in cell body upper edge, avoids waste and pollutes.
In conjunction with the accompanying drawings embodiment of the present utility model is specified above, but the utility model is not limited to the foregoing description, in the ken that those of ordinary skills possessed, can also make various variations not breaking away under the utility model aim prerequisite.

Claims (4)

1. tar wood vinegar separator, it is characterized in that: described separator comprises the casing of a bottom surface level, described casing internal fixing has dividing plate (5), the top margin of described dividing plate (5) is lower than the end face of casing, described dividing plate (5) is divided into disconnected first separator tank (1) and (2) two inner chambers of second separator tank with casing, described separator also comprises liquid-inlet pipe (3), tar delivery line (8) and wood vinegar delivery line (9), the top of described first separator tank (1) is communicated with liquid-inlet pipe (3), the bottom is provided with the pipeline that is connected with tar delivery line (8), be connected with the first separator tank valve (6) on the pipeline between described first separator tank (1) and the tar delivery line (8), the top of described second separator tank (2) is communicated with wood vinegar delivery line (9), the bottom is provided with the pipeline that is connected with tar delivery line (8), is connected with the second separator tank valve (7) on the pipeline between described second separator tank (2) and the tar delivery line (8).
2. a kind of tar wood vinegar separator according to claim 1, it is characterized in that: the casing of described separator is a rectangular parallelepiped.
3. a kind of tar wood vinegar separator according to claim 1 is characterized in that: the volume of described first separator tank (1) and second separator tank (2) equates.
4. a kind of tar wood vinegar separator according to claim 1, it is characterized in that: the height of described dividing plate (5) is 70%~90% of a box height.
CN2011201580701U 2011-05-18 2011-05-18 Tar wood vinegar separator Expired - Fee Related CN202039029U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011201580701U CN202039029U (en) 2011-05-18 2011-05-18 Tar wood vinegar separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011201580701U CN202039029U (en) 2011-05-18 2011-05-18 Tar wood vinegar separator

Publications (1)

Publication Number Publication Date
CN202039029U true CN202039029U (en) 2011-11-16

Family

ID=44966484

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011201580701U Expired - Fee Related CN202039029U (en) 2011-05-18 2011-05-18 Tar wood vinegar separator

Country Status (1)

Country Link
CN (1) CN202039029U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103184096A (en) * 2012-01-01 2013-07-03 湖南绿步科技有限责任公司 Vegetable fat distillation method capable of improving production efficiency and auxiliary equipment
CN105950191A (en) * 2016-04-19 2016-09-21 咸阳盘州现代农业有限公司 Integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating
CN115721971A (en) * 2023-01-10 2023-03-03 邢台市茂新化工产品有限公司 Automatic ester-water separator for butyl acetate production

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103184096A (en) * 2012-01-01 2013-07-03 湖南绿步科技有限责任公司 Vegetable fat distillation method capable of improving production efficiency and auxiliary equipment
CN105950191A (en) * 2016-04-19 2016-09-21 咸阳盘州现代农业有限公司 Integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating
CN115721971A (en) * 2023-01-10 2023-03-03 邢台市茂新化工产品有限公司 Automatic ester-water separator for butyl acetate production

Similar Documents

Publication Publication Date Title
CN201865755U (en) Biogas power generation system
AU2020100952A4 (en) An Anaerobic Digestion Device For Strengthening Biogas Production By Self-Sustaining Air Floatation
CN202039029U (en) Tar wood vinegar separator
CN201695028U (en) Inner-container-type external circulating solar biogas digester
CN204125315U (en) A kind of plant biogas fermentation device
CN103087902B (en) Automatic crusting-breaking gas producing and storing wet type integrated anaerobic fermentation device
CN104293654A (en) Novel biogas digester
CN210974668U (en) Clear water compressed-air methane tank
CN201427968Y (en) Top and bottom internal recycle biomass pool
CN205295323U (en) Water pressure type slag liquid automatic circulation methane tank
CN206143193U (en) Family is with two air storage fermenting installation of marsh gas
CN106148170A (en) The double air storage installation for fermenting of household biogas
CN101654688B (en) Device for efficiently producing marsh gas
CN206089670U (en) Feed liquid circulation fluidization fermenting installation
CN205821316U (en) Association type biogas stirring device
CN204569913U (en) For the feeding unit of stalk anaerobic fermentation gas making
CN102876566A (en) Upper-baffled straw type mobile methane fermentation tank
CN203668382U (en) Biogas power generation and burning utilization system
CN203668389U (en) Fermentation and gas storage device of biogas power generation and burning utilization system
CN203096068U (en) Automatic shell-breaking gas producing and storing wet type integrated anaerobic fermenting device
CN204198732U (en) A kind of simple and easy biogas fermentation device
CN102464439A (en) Methane pressure stabilizing device and manufacturing process thereof
CN203715626U (en) System for fermenting biogas by utilizing kitchen waste oil
CN203668384U (en) Gas storage device of biogas power generation and burning utilization system
CN211522181U (en) High-concentration composite functional methane tank

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20111116

Termination date: 20150518

EXPY Termination of patent right or utility model