CN201832450U - Separation device for producing liquid by using biomass through dry distillation - Google Patents
Separation device for producing liquid by using biomass through dry distillation Download PDFInfo
- Publication number
- CN201832450U CN201832450U CN2010205353971U CN201020535397U CN201832450U CN 201832450 U CN201832450 U CN 201832450U CN 2010205353971 U CN2010205353971 U CN 2010205353971U CN 201020535397 U CN201020535397 U CN 201020535397U CN 201832450 U CN201832450 U CN 201832450U
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- Prior art keywords
- input pipe
- liquid outlet
- liquid
- section
- primary input
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- 239000007788 liquid Substances 0.000 title claims abstract description 113
- 239000002028 Biomass Substances 0.000 title claims abstract description 10
- 238000000926 separation method Methods 0.000 title abstract description 9
- 238000000197 pyrolysis Methods 0.000 title abstract description 3
- 238000003763 carbonization Methods 0.000 claims description 8
- 238000011084 recovery Methods 0.000 claims description 4
- 239000011276 wood tar Substances 0.000 description 18
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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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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- Coke Industry (AREA)
Abstract
The utility model discloses a separation device for producing liquid by using biomass through dry distillation, which comprises a separation kettle I. An input pipe is arranged above the separation kettle I and comprises a main input pipe, a diversion pipe and a vertical pipe. The main input pipe comprises a main input pipe section A and a main input pipe section B which is connected with the main input pipe section A through a T-joint, wherein the main input pipe section B is provided with a check valve. The diversion pipe is arranged above the main input pipe section B. One end of the diversion pipe is connected with the vertical end of the T-joint. The vertical pipe vertically stretches into the separation kettle and is sequentially connected with the other end of the diversion pipe and one end of the main input pipe section B far away from the T-joint. A liquid outlet I, a liquid outlet II and a liquid outlet III are respectively arranged at the bottom, the middle part and the upper part of the separation kettle I. The separation device has the advantages that the flow and the flow rate of the liquid entering the separation kettle I can be controlled, the liquid can be purified and separated, the structure is simple, the device is convenient to use and the popularization and the application are facilitated.
Description
Technical field
The utility model relates to a kind of separator, particularly a kind of separator that is used for biomass carbonization generation liquid object.
Background technology
When living beings can produce liquids such as pyrolkigneous liquid and wood tar after destructive distillation, need carry out separated and collected to these liquids, existing liquid towards thing is collected when separating, be liquid object to be directly inputted in the container leave standstill, but in practical operation, when being input to liquid object in the container, the flow of the liquid object in the uncontrollable feeding gathering-device pipeline, cause the flow of pipeline inflow gathering-device bigger, flow velocity is accelerated, in actual production process, other relevant production procedure is impacted, use very inconvenient.And it is when adopting standing methods to separate, consuming time oversize.
The utility model content
The purpose of this utility model is to overcome above-mentioned deficiency of the prior art, and a kind of separator that biomass carbonization produces liquid object that is used for is provided.The utility model can be controlled flow and the flow velocity that liquid object enters separating still, and it is simple in structure, easy to use, good stability, production cost are low, is convenient to promote the use of.
For achieving the above object, the technical solution adopted in the utility model is: be used for the separator that biomass carbonization produces liquid object, it is characterized in that: comprise separating still one, the top of described separating still one is provided with input pipe, described input pipe comprises the primary input pipe, isocon and vertical tube, described primary input pipe comprises primary input pipe A section and the primary input pipe B section that is connected with primary input pipe A section by three-way connection, and described primary input pipe B section is provided with check valve, described isocon is arranged on the top of primary input pipe B section, and an end of described isocon is connected with the vertical end of three-way connection, described vertical tube vertically extends in the separating still and successively the other end of isocon and primary input pipe B section is connected the bottom of described separating still one away from an end of three-way connection, middle part and top are respectively arranged with liquid outlet one, liquid outlet two and liquid outlet three.
The above-mentioned separator that is used for biomass carbonization generation liquid object, described liquid outlet two is connected with separating still two, the bottom of described separating still two, middle part and top are respectively arranged with liquid outlet four, liquid outlet five, liquid outlet six, described liquid outlet four belows are provided with the recovery trunk line, described recovery trunk line is connected liquid outlet one successively with liquid outlet four, the position of described liquid outlet three is higher than the position that liquid outlet two is connected with separating still two.
The utility model compared with prior art has the following advantages: the utility model is higher than the isocon of primary input pipe B section by setting, reduced the pressure reduction that flows into liquid object in the separating still, guarantee to maintain liquid object in the primary input pipe A section always, can not produce air, the flow and the flow velocity of energy better controlled liquid object, and the utility model has utilized the characteristic of interior pyrolkigneous liquid of liquid object and wood tar, cleverly the pyrolkigneous liquid in the liquid object is purified with wood tar and separate, can also carry out multi-stage separation, with dna purity higher pyrolkigneous liquid and wood tar.Of the present utility model simple in structure, easy to use, very big practical value is arranged.
Below by drawings and Examples, the technical solution of the utility model is described in further detail.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model.
Description of reference numerals:
1-primary input pipe; 2-primary input pipe A section; The 3-three-way connection;
The 4-check valve; The 5-isocon; 6-primary input pipe B section;
The 7-vertical tube; The 8-wood tar that floats; 9-separating still one;
The 10-pyrolkigneous liquid; 11-sinking wood tar; 12-liquid outlet one;
13-liquid outlet three; 14-reclaims trunk line; 15-liquid outlet two;
16-liquid outlet four; 17-liquid outlet five; 18-separating still two;
19-liquid outlet six.
The specific embodiment
A kind of separator that is used for biomass carbonization generation liquid object as shown in Figure 1, comprise separating still 1, the top of described separating still 1 is provided with input pipe, described input pipe comprises primary input pipe 1, isocon 5 and vertical tube 7, described primary input pipe 1 comprises primary input pipe A section 2 and the primary input pipe B section 6 that is connected with primary input pipe A section 2 by three-way connection 3, and described primary input pipe B section 6 is provided with check valve 4, described isocon 5 is arranged on the top of primary input pipe B section 6, and an end of described isocon 5 is connected with the vertical end of three-way connection 3, described vertical tube 7 vertically extends in the separating still 9 and successively the other end of isocon 5 and primary input pipe B section 6 is connected the bottom of described separating still 1 away from an end of three-way connection 3, middle part and top are respectively arranged with liquid outlet 1, liquid outlet 2 15 and liquid outlet 3 13.
During use, primary input pipe A section 2 is connected with the liquid object delivery outlet of distillation apparatus, close check valve 4, described liquid object is by primary input pipe A section 2, because so check valve 4 is closed primary input pipe B section 6 and is blocked, so, liquid object is input to isocon 5 through three-way connection 3, liquid object is input to the separating still 1 from isocon 5 through vertical tube 7 then, because isocon 5 is positioned at the top of primary input pipe B section 6, be that isocon 5 is higher than primary input pipe B section 6 on vertical position, and primary input pipe B section 6 and primary input pipe A section 2 are positioned on the same horizontal plane, during use, close check valve 4, liquid object enters isocon 5 and enters in the separating still 1 through vertical tube 7, adopt this mode, can reduce flow and flow velocity that liquid object flows into separating still 1, reduced to flow into the pressure reduction of liquid object in the separating still 9, guarantee to maintain liquid object in the primary input pipe A section 2 always, can not produce air, the flow and the flow velocity of energy better controlled liquid object, when liquids will soon have flowed, open check valve 4, promptly connect primary input pipe A section 2 and primary input pipe B section 6, liquid object directly flows to primary input pipe B section 6 from primary input pipe A section 2, and then enter in the separating still 1 through vertical tube 7, after liquid object enters separating still 1, liquid object utilizes its proportion to separate voluntarily in separating still, wherein a part of wood tar floats to the top of separating still 1, part wood tar sinks down into the bottom of separating still 1, other pyrolkigneous liquid 10 is positioned at the middle part of separating still 1, be designated as come-up wood tar 8 respectively, pyrolkigneous liquid 10 and sinking wood tar 11, come-up wood tar 8 is exported the back and is stored from liquid outlet 3 13, sinking wood tar 11 stores by output back in the liquid outlet 1, pyrolkigneous liquid 10 stores by output back in the liquid outlet 2 15, described liquid outlet 1, liquid outlet 2 15 and liquid outlet 3 13 are provided with the valve that control liquid flows out, utilize wood tar with the pyrolkigneous liquid self characteristics wood tar in the liquid object to be separated with pyrolkigneous liquid, it is very convenient to use.
As further improvement, described liquid outlet 2 15 is connected with separating still 2 18, the bottom of described separating still 2 18, middle part and top are respectively arranged with liquid outlet 4 16, liquid outlet 5 17, liquid outlet 6 19, described liquid outlet 4 16 belows are provided with reclaims trunk line 14, described recovery trunk line 14 is connected liquid outlet 1 successively with liquid outlet 4 16, the position of described liquid outlet 3 13 is higher than the position that liquid outlet 2 15 is connected with separating still 2 18, liquid outlet 4 16, liquid outlet 5 17 and liquid outlet 6 19 are provided with the valve that control liquid flows out.
Be connected with separating still 2 18 by liquid outlet 2 15, pyrolkigneous liquid 10 is input in the separating still 2 18, residual wood tar in the pyrolkigneous liquid 10 further separates in separating still 2 18, the wood tar of come-up is from liquid outlet 6 19 outputs and storage, the wood tar that sinks flows into from liquid outlet 16 and reclaims trunk line 14, and the pyrolkigneous liquid 10 that is arranged in separating still 2 18 middle parts is from liquid outlet 5 17 outputs and storage.Separate by the secondary of liquids is purified, obtained higher wood tar and the pyrolkigneous liquid of purity.
The above; it only is preferred embodiment of the present utility model; be not that the utility model is imposed any restrictions; every according to the utility model technical spirit to any simple modification, change and equivalent structure transformation that above embodiment did, all still belong in the protection domain of technical solutions of the utility model.
Claims (2)
1. be used for the separator that biomass carbonization produces liquid object, it is characterized in that: comprise separating still one (9), the top of described separating still one (9) is provided with input pipe, described input pipe comprises primary input pipe (1), isocon (5) and vertical tube (7), described primary input pipe (1) comprises primary input pipe A section (2) and the primary input pipe B section (6) that is connected with primary input pipe A section (2) by three-way connection (3), and described primary input pipe B section (6) is provided with check valve (4), described isocon (5) is arranged on the top of primary input pipe B section (6), and an end of described isocon (5) is connected with the vertical end of three-way connection (3), described vertical tube (7) vertically extends in the separating still (9) and successively the other end of isocon (5) is connected the bottom of described separating still one (9) with the end of primary input pipe B section (6) away from three-way connection (3), middle part and top are respectively arranged with liquid outlet one (12), liquid outlet two (15) and liquid outlet three (13).
2. the separator that is used for biomass carbonization generation liquid object according to claim 1, it is characterized in that: described liquid outlet two (15) is connected with separating still two (18), the bottom of described separating still two (18), middle part and top are respectively arranged with liquid outlet four (16), liquid outlet five (17), liquid outlet six (19), described liquid outlet four (16) belows are provided with reclaims trunk line (14), described recovery trunk line (14) is connected liquid outlet one (12) successively with liquid outlet four (16), the position of described liquid outlet three (13) is higher than the position that liquid outlet two (15) is connected with separating still two (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205353971U CN201832450U (en) | 2010-09-17 | 2010-09-17 | Separation device for producing liquid by using biomass through dry distillation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205353971U CN201832450U (en) | 2010-09-17 | 2010-09-17 | Separation device for producing liquid by using biomass through dry distillation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201832450U true CN201832450U (en) | 2011-05-18 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205353971U Expired - Fee Related CN201832450U (en) | 2010-09-17 | 2010-09-17 | Separation device for producing liquid by using biomass through dry distillation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201832450U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108865200A (en) * | 2018-07-02 | 2018-11-23 | 安徽省建辉生物质能发展有限公司 | A kind of device for effectively separating for biomass wood tar and wood vinegar |
-
2010
- 2010-09-17 CN CN2010205353971U patent/CN201832450U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108865200A (en) * | 2018-07-02 | 2018-11-23 | 安徽省建辉生物质能发展有限公司 | A kind of device for effectively separating for biomass wood tar and wood vinegar |
| CN108865200B (en) * | 2018-07-02 | 2020-07-24 | 安徽省建辉生物质能发展有限公司 | A high-efficient separator for living beings wood tar and pyrolkigneous liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Separation device for producing liquid by using biomass through dry distillation Effective date of registration: 20130816 Granted publication date: 20110518 Pledgee: Yangling Shaanxi rural commercial bank Limited by Share Ltd Pledgor: Shaanxi Yixin Biological Energy Science and Technology Development Co., Ltd. Registration number: 2013990000588 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20150813 Granted publication date: 20110518 Pledgee: Yangling Shaanxi rural commercial bank Limited by Share Ltd Pledgor: Shaanxi Yixin Biological Energy Science and Technology Development Co., Ltd. Registration number: 2013990000588 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Separation device for producing liquid by using biomass through dry distillation Effective date of registration: 20150906 Granted publication date: 20110518 Pledgee: Yangling Shaanxi rural commercial bank Limited by Share Ltd Pledgor: Shaanxi Yixin Biological Energy Science and Technology Development Co., Ltd. Registration number: 2015610000014 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20190328 Granted publication date: 20110518 Pledgee: Yangling Shaanxi rural commercial bank Limited by Share Ltd Pledgor: Shaanxi Yixin Biological Energy Science and Technology Development Co., Ltd. Registration number: 2015610000014 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Separation device for producing liquid by using biomass through dry distillation Effective date of registration: 20190409 Granted publication date: 20110518 Pledgee: Yangling Shaanxi rural commercial bank Limited by Share Ltd Pledgor: Shaanxi Yixin Biological Energy Science and Technology Development Co., Ltd. Registration number: 2019610000062 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110518 Termination date: 20190917 |