CN204138658U - With the heating unit of cavity - Google Patents
With the heating unit of cavity Download PDFInfo
- Publication number
- CN204138658U CN204138658U CN201420464148.6U CN201420464148U CN204138658U CN 204138658 U CN204138658 U CN 204138658U CN 201420464148 U CN201420464148 U CN 201420464148U CN 204138658 U CN204138658 U CN 204138658U
- Authority
- CN
- China
- Prior art keywords
- biogas
- introduction channel
- elementary
- cylindrical container
- scatterer
- 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
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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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
A kind of heating unit with cavity, described heating unit is with the cylindrical container of cavity, well heater, comprise the scatterer of heat pipe, water-atomization cooling equipment, for the introduction channel of marsh gas raw materials, for the introduction channel of air, the elementary introduction channel of biogas, the elementary derivation passage of biogas, the secondary introduction channel of biogas, the secondary of biogas derives passage, cylindrical container enter aquaporin, the derivation passage of gas, the introduction channel of cooling water smoke, the flow pass of scavenging solution, three grades of export mouths of biogas, the elementary pipeline of biogas and the secondary canalization of biogas, such structure avoids the defect causing the increase of a large amount of expenses and the difficulty of accessory device maintenance of prior art.
Description
Technical field
The utility model belongs to heating device technology area, is specifically related to a kind of heating unit with cavity.
Background technology
Stalk, weeds are as marsh gas raw materials, the proportion formed methane is about 60%, the main composition part of Ye Shi rural households fuel, because such marsh gas raw materials collects easy and that organic material component is not low advantage, fermentation process under only needing a small amount of marsh gas raw materials to heat in back transfer process just can realize the generation of biogas, generation method like this has the biogas generation method of expanding type biogas generation method and the granulating marsh gas raw materials before expanding type biogas generation method, without exception all to adopt stalk, the such marsh gas raw materials of weeds is sent to by the head of the heating unit of marsh gas raw materials, then order via dryer, thermal degradation system, sludge gas collecting device, Upper separator, Lower separator and residual particulate matter collection container, such biogas removes by particulate matter state after generating, the flowing of biogas is reciprocal flowing, through hole above dryer flows out, method can realize drying and thermal degradation among thermal degradation terminates thus, the heat that biogas finally can be allowed to generate keeps controlled in the state that biogas generates, and can recycle discharge biogas energy, improve utilization ratio, but toxic liquid can be discharged in the implementation procedure of the oven dry of putting due to the heating of such marsh gas raw materials and thermal degradation and toxic gas is mixed in biogas, in addition in Upper separator realize leading in purifying and cooling into scavenging solution in also can add generation toxic liquid, many sulfide and nitride is comprised in toxic liquid, purification difficulty, through test, often use 500 kilograms of marsh gas raw materials, the toxic liquid of 12000 milligrams often liter generally will be reached along with 500 kilograms of sulfide and nitride, if carry out purifying treatment, the increase of a large amount of expenses and the difficulty of accessory device maintenance can be caused with current level of purification.
Utility model content
The purpose of this utility model provides a kind of heating unit with cavity, described heating unit is with the cylindrical container of cavity, well heater, comprise the scatterer of heat pipe, water-atomization cooling equipment, for the introduction channel of marsh gas raw materials, for the introduction channel of air, the elementary introduction channel of biogas, the elementary derivation passage of biogas, the secondary introduction channel of biogas, the secondary of biogas derives passage, cylindrical container enter aquaporin, the derivation passage of gas, the introduction channel of cooling water smoke, the flow pass of scavenging solution, three grades of export mouths of biogas, the elementary pipeline of biogas and the secondary canalization of biogas, the outer wall of described cylindrical container is provided with coiled metal pipes, the upper end of cylindrical container 1 is installed with the introduction channel for marsh gas raw materials, residual particulate matter collection container is installed from low to high successively in the inside of described cylindrical container 1, Lower separator, Upper separator, sludge gas collecting device, thermal degradation system and dryer, the inside of described cylindrical container is installed with well heater, the top of described well heater offers the elementary introduction channel of biogas, the below of described elementary introduction channel is the dryer in cylindrical container, the lower end of described well heater is the elementary derivation passage of biogas, the position of the elementary derivation passage of described biogas is above thermal degradation system, the outer surface of cylindrical container is installed with the introduction channel for air, the outer wall of described cylindrical container is installed with the scatterer comprising heat pipe, the described lower end comprising the scatterer of heat pipe is installed with the secondary introduction channel of biogas, the secondary introduction channel of biogas is connected with the elementary derivation passage of biogas through the elementary pipeline of biogas, the upper end of the described scatterer 3 comprising heat pipe is installed with the secondary derivation passage of biogas, the secondary canalization of described biogas is connected with water-atomization cooling equipment through the secondary canalization of biogas, the derivation passage entering aquaporin and gas of cylindrical container is installed above and below the described outside surface comprising the scatterer of heat pipe separately, the top and bottom of described water-atomization cooling equipment are installed with the introduction channel of cooling water smoke and the flow pass of scavenging solution respectively, the outside surface on one side of described water-atomization cooling equipment 4 is provided with three grades of export mouths of biogas.Such structure avoids the defect causing the increase of a large amount of expenses and the difficulty of accessory device maintenance of prior art.
In order to overcome deficiency of the prior art, the utility model provides a kind of solution of the heating unit with cavity, specific as follows:
A kind of heating unit with cavity, described heating unit is with the cylindrical container 1 of cavity, well heater 2, comprise the scatterer 3 of heat pipe, water-atomization cooling equipment 4, for the introduction channel 5 of marsh gas raw materials, for the introduction channel 6 of air, the elementary introduction channel 7 of biogas, the elementary derivation passage 8 of biogas, the secondary introduction channel 9 of biogas, the secondary of biogas derives path 10, cylindrical container enter aquaporin 11, the derivation passage 12 of gas, the introduction channel 13 of cooling water smoke, the flow pass 14 of scavenging solution, three grades of export mouths 15 of biogas, the elementary pipeline 16 of biogas and the secondary canalization 17 of biogas, the outer wall of described cylindrical container 1 is provided with coiled metal pipes, the upper end of cylindrical container 1 is installed with the introduction channel 5 for marsh gas raw materials, residual particulate matter collection container 18 is installed from low to high successively in the inside of described cylindrical container 1, Lower separator 19, Upper separator 20, sludge gas collecting device 21, thermal degradation system 22 and dryer 23, the inside of described cylindrical container 1 is installed with well heater 2, the top of described well heater 2 offers the elementary introduction channel 7 of biogas, the below of described elementary introduction channel 7 is the dryer 23 in cylindrical container 1, the lower end of described well heater 2 is the elementary derivation passage 8 of biogas, the position of the elementary derivation passage 8 of described biogas is above thermal degradation system 22, the outer surface of cylindrical container 1 is installed with the introduction channel 6 for air, the outer wall of described cylindrical container 1 is installed with the scatterer 3 comprising heat pipe, the lower end of the described scatterer 3 comprising heat pipe is installed with the secondary introduction channel 9 of biogas, the secondary introduction channel 9 of biogas is connected with the elementary derivation passage 8 of biogas through the elementary pipeline 16 of biogas, the upper end of the described scatterer 3 comprising heat pipe is installed with the secondary derivation path 10 of biogas, the secondary canalization 17 of described biogas is connected with water-atomization cooling equipment 4 through the secondary canalization 17 of biogas, the derivation passage 12 entering aquaporin 11 and gas of cylindrical container is installed above and below the outside surface of the described scatterer 3 comprising heat pipe separately, the top and bottom of described water-atomization cooling equipment 4 are installed with the introduction channel 13 of cooling water smoke and the flow pass 14 of scavenging solution respectively, the outside surface on one side of described water-atomization cooling equipment 4 is provided with three grades of export mouths 15 of biogas.
Described well heater 2 is tubular or prism-shaped.
Described well heater 2 is installed on the interior surface of cylindrical container 1.
The described scatterer 3 comprising heat pipe can be installed on coiled metal pipes.
Application the utility model such scheme, tool has the following advantages:
Substantially reduce the waste liquid of biogas cleaning and the generation of waste gas, the generation formed methane can also be configured through structural changes, make the device side of link below to the needs of the generation content of biogas, such device form is uncomplicated, expense is not high, biogas constructive system maintainability is good, and can reduce waste liquid and the waste gas of biogas cleaning.
Accompanying drawing explanation
Fig. 1 is sectional structure schematic diagram of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, utility model content is described further:
With reference to shown in Fig. 1, with the heating unit of cavity, described heating unit is with the cylindrical container 1 of cavity, well heater 2, comprise the scatterer 3 of heat pipe, water-atomization cooling equipment 4, for the introduction channel 5 of marsh gas raw materials, for the introduction channel 6 of air, the elementary introduction channel 7 of biogas, the elementary derivation passage 8 of biogas, the secondary introduction channel 9 of biogas, the secondary of biogas derives path 10, cylindrical container enter aquaporin 11, the derivation passage 12 of gas, the introduction channel 13 of cooling water smoke, the flow pass 14 of scavenging solution, three grades of export mouths 15 of biogas, the elementary pipeline 16 of biogas and the secondary canalization 17 of biogas, the outer wall of described cylindrical container 1 is provided with coiled metal pipes, the upper end of cylindrical container 1 is installed with the introduction channel 5 for marsh gas raw materials, residual particulate matter collection container 18 is installed from low to high successively in the inside of described cylindrical container 1, Lower separator 19, Upper separator 20, sludge gas collecting device 21, thermal degradation system 22 and dryer 23, the inside of described cylindrical container 1 is installed with well heater 2, described well heater 2 is used for gathering elementary biogas and initial gross separation goes out elementary biogas, the top of described well heater 2 offers the elementary introduction channel 7 of biogas, the below of described elementary introduction channel 7 is the dryer 23 in cylindrical container 1, the lower end of described well heater 2 is the elementary derivation passage 8 of biogas, the position of the elementary derivation passage 8 of described biogas is above thermal degradation system 22, the outer surface of cylindrical container 1 is installed with the introduction channel 6 for air, the outer wall of described cylindrical container 1 is installed with the scatterer 3 comprising heat pipe, the lower end of the described scatterer 3 comprising heat pipe is installed with the secondary introduction channel 9 of biogas, the secondary introduction channel 9 of biogas is connected with the elementary derivation passage 8 of biogas through the elementary pipeline 16 of biogas, the upper end of the described scatterer 3 comprising heat pipe is installed with the secondary derivation path 10 of biogas, the secondary canalization 17 of described biogas is connected with water-atomization cooling equipment 4 through the secondary canalization 17 of biogas, the derivation passage 12 entering aquaporin 11 and gas of cylindrical container is installed above and below the outside surface of the described scatterer 3 comprising heat pipe separately, the top and bottom of described water-atomization cooling equipment 4 are installed with the introduction channel 13 of cooling water smoke and the flow pass 14 of scavenging solution respectively, such cooling liqs just can be sent through the flow pass 14 of scavenging solution through water-atomization cooling equipment 4 again and repeatedly use, the outside surface on one side of described water-atomization cooling equipment 4 is provided with three grades of export mouths 15 of biogas, biogas like this after cleaning just can pass out to another link.Described well heater 2 is tubular or prism-shaped.Described well heater 2 is installed on the interior surface of cylindrical container 1.The described scatterer 3 comprising heat pipe can be installed on coiled metal pipes.
When principle of work of the present utility model is initial, marsh gas raw materials is inserted in cylindrical container 1 through the introduction channel 5 for marsh gas raw materials, and air is inputted from the introduction channel 6 for air, such air and marsh gas raw materials first generate elementary biogas in cylindrical container, after the elementary introduction channel 7 of biogas gathers elementary biogas, elementary biogas is led and then to heat up the decomposition carried out sulfide and nitride into well heater 2, derive from the elementary derivation passage 8 of biogas again, the biogas of deriving from the elementary derivation passage 8 of biogas enters through the elementary pipeline 16 of biogas and comprises the scatterer 3 of heat pipe, derivation passage 12 again through gas after heat pipe cooling discharges the fluid of vaporization, obtain the biogas after cooling, biogas after cooling sends into water-atomization cooling equipment 4 after the secondary of biogas derives path 10 outflow, biogas after cleaning flows out through three grades of export mouths 15 of biogas, and scavenging solution is discharged through the flow pass 14 of scavenging solution.
By facts have proved, the methane content produced with device of the present utility model can increase by more than 25%, and often uses 500 kilograms of marsh gas raw materials, and the content of toxic liquid is reduced to often liter less than 300 milligrams.
The above, it is only preferred embodiment of the present utility model, not any pro forma restriction is done to the utility model, although the utility model discloses as above with preferred embodiment, but and be not used to limit the utility model, any those skilled in the art, do not departing within the scope of technical solutions of the utility model, make a little change when the technology contents of above-mentioned announcement can be utilized or be modified to the Equivalent embodiments of equivalent variations, in every case be do not depart from technical solutions of the utility model content, according to technical spirit of the present utility model, within spirit of the present utility model and principle, to any simple amendment that above embodiment is done, equivalent replacement and improvement etc., within the protection domain all still belonging to technical solutions of the utility model.
Claims (4)
1. the heating unit with cavity, it is characterized in that the cylindrical container of described heating unit with cavity, well heater, comprise the scatterer of heat pipe, water-atomization cooling equipment, for the introduction channel of marsh gas raw materials, for the introduction channel of air, the elementary introduction channel of biogas, the elementary derivation passage of biogas, the secondary introduction channel of biogas, the secondary of biogas derives passage, cylindrical container enter aquaporin, the derivation passage of gas, the introduction channel of cooling water smoke, the flow pass of scavenging solution, three grades of export mouths of biogas, the elementary pipeline of biogas and the secondary canalization of biogas, the outer wall of described cylindrical container is provided with coiled metal pipes, the upper end of cylindrical container is installed with the introduction channel for marsh gas raw materials, residual particulate matter collection container is installed from low to high successively in the inside of described cylindrical container, Lower separator, Upper separator, sludge gas collecting device, thermal degradation system and dryer, the inside of described cylindrical container is installed with well heater, the top of described well heater offers the elementary introduction channel of biogas, the below of described elementary introduction channel is the dryer in cylindrical container, the lower end of described well heater is the elementary derivation passage of biogas, the position of the elementary derivation passage of described biogas is above thermal degradation system, the outer surface of cylindrical container is installed with the introduction channel for air, the outer wall of described cylindrical container is installed with the scatterer comprising heat pipe, the described lower end comprising the scatterer of heat pipe is installed with the secondary introduction channel of biogas, the secondary introduction channel of biogas is connected with the elementary derivation passage of biogas through the elementary pipeline of biogas, the secondary that the described upper end comprising the scatterer of heat pipe is installed with biogas derives passage, the secondary canalization of described biogas is connected with water-atomization cooling equipment through the secondary canalization of biogas, the derivation passage entering aquaporin and gas of cylindrical container is installed above and below the described outside surface comprising the scatterer of heat pipe separately, the top and bottom of described water-atomization cooling equipment are installed with the introduction channel of cooling water smoke and the flow pass of scavenging solution respectively, the outside surface on one side of described water-atomization cooling equipment is provided with three grades of export mouths of biogas.
2. the heating unit with cavity according to claim 1, is characterized in that described well heater is tubular or prism-shaped.
3. the heating unit with cavity according to claim 1, is characterized in that described well heater is installed on the interior surface of cylindrical container.
4. the heating unit with cavity according to claim 1, is characterized in that the described scatterer comprising heat pipe can be installed on coiled metal pipes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420464148.6U CN204138658U (en) | 2014-08-18 | 2014-08-18 | With the heating unit of cavity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420464148.6U CN204138658U (en) | 2014-08-18 | 2014-08-18 | With the heating unit of cavity |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204138658U true CN204138658U (en) | 2015-02-04 |
Family
ID=52415358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420464148.6U Expired - Fee Related CN204138658U (en) | 2014-08-18 | 2014-08-18 | With the heating unit of cavity |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204138658U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105713826A (en) * | 2014-08-19 | 2016-06-29 | 姚小兵 | Heating device with cavity |
-
2014
- 2014-08-18 CN CN201420464148.6U patent/CN204138658U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105713826A (en) * | 2014-08-19 | 2016-06-29 | 姚小兵 | Heating device with cavity |
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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: 20150204 Termination date: 20150818 |
|
| EXPY | Termination of patent right or utility model |