CN105713826A - Heating device with cavity - Google Patents
Heating device with cavity Download PDFInfo
- Publication number
- CN105713826A CN105713826A CN201410407462.5A CN201410407462A CN105713826A CN 105713826 A CN105713826 A CN 105713826A CN 201410407462 A CN201410407462 A CN 201410407462A CN 105713826 A CN105713826 A CN 105713826A
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- CN
- China
- Prior art keywords
- biogas
- primary
- cylindrical container
- heater
- introduction channel
- 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.)
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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
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses a heating device with a cavity. The heating device is provided with a tubular container with a cavity, a heater, a radiator comprising a heat pipe, water mist cooling equipment, a lead-in channel for a marsh gas material, a lead-in channel for air, a primary lead-in channel of a marsh gas, a primary lead-out channel of a marsh gas, a secondary lead-in channel of a marsh gas, a secondary lead-out channel of a marsh gas, a water inlet channel of the tubular container, a lead-out channel of a gas, a lead-in channel of water spray for cooling, an outflow channel of cleanout fluid, a three-stage lead-out opening of a marsh gas, a primary pipeline of a marsh gas and a secondary pipeline of a marsh gas. The defects of a great increase of the cost and maintenance difficulty of attached device in the prior art are avoided by the structure.
Description
Technical field
The invention belongs to heating device technology area, be specifically related to a kind of heater with cavity.
Background technology
Straw, 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 the advantage that such marsh gas raw materials is collected easily and organic material component is not low, have only to the fermentation process under a small amount of marsh gas raw materials is heated in back transfer process and can be realized as the generation of biogas, generation method like this has the biogas that expansion type biogas generates method and the granulating marsh gas raw materials before expansion type biogas generation method to generate method, without exception will adopt straw, the such marsh gas raw materials of weeds is sent into by the head of the heater of marsh gas raw materials, then order via dehydrator, heat resolve system, sludge gas collecting device, Upper separator, Lower separator and residual particulate matter collect container, such biogas removes by particulate matter state after generating, the flowing of biogas is reciprocal flowing, through hole above dehydrator flows out, thus method can realize drying and heat resolve among heat resolve terminates, the heat that biogas generates finally can be allowed to keep controlled in the state that biogas generates, and the biogas energy of discharge can be recycled, improve utilization rate, the realizing of the drying put yet with the heating of such marsh gas raw materials and heat resolve can discharge toxic liquid in process and toxic gas is mixed in biogas, additionally in Upper separator realize purifying and cooling is led into cleanout fluid in also can add generation toxic liquid, many sulfide and nitride is included in toxic liquid, purify difficulty, through test, often use 500 kilograms of marsh gas raw materials, the toxic liquid of 12000 milligrams every liter generally will be reached along with 500 kilograms of sulfide and nitride, if carried out purified treatment, the increase of substantial amounts of expense and the difficulty of accessory device maintenance can be caused with current level of purification.
Summary of the invention
It is an object of the invention to provide a kind of heater with cavity, described heater is with the cylindrical container of cavity, heater, radiator including heat pipe, water-atomization cooling equipment, introduction channel for marsh gas raw materials, introduction channel for air, the primary introduction channel of biogas, the primary of biogas derives passage, two grades of introduction channels of biogas, two grades of biogas derive passage, cylindrical container enter aquaporin, the derivation passage of gas, the introduction channel of cooling water smoke, the flow pass of cleanout fluid, three grades of export mouths of biogas, the primary 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, the inside of described cylindrical container 1 is installed residual particulate matter from low to high successively and is collected container, Lower separator, Upper separator, sludge gas collecting device, heat resolve system and dehydrator, internally installed the heater of described cylindrical container, the top of described heater offers the primary introduction channel of biogas, the lower section of described primary introduction channel is the dehydrator in cylindrical container, the primary that the lower end of described heater is biogas derives passage, the primary of described biogas derives the position of passage above heat resolve 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 radiator including heat pipe, the lower end of the described radiator including heat pipe is installed with two grades of introduction channels of biogas, two grades of introduction channels of biogas are connected with the primary derivation passage of biogas through the primary pipeline of biogas, the upper end of the described radiator 3 including heat pipe is installed with two grades of derivation passages 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 each installed above and below the outer surface of the described radiator including heat pipe, the top and bottom of described water-atomization cooling equipment are respectively mounted the introduction channel of cooling water smoke and the flow pass of cleanout fluid, the outer 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 increase causing substantial amounts of expense of prior art and the defect of the difficulty of accessory device maintenance.
In order to overcome deficiency of the prior art, the invention provides the solution of a kind of heater with cavity, specific as follows:
A kind of heater with cavity, described heater is with the cylindrical container 1 of cavity, heater 2, radiator 3 including heat pipe, water-atomization cooling equipment 4, introduction channel 5 for marsh gas raw materials, introduction channel 6 for air, the primary introduction channel 7 of biogas, the primary of biogas derives passage 8, two grades of introduction channels 9 of biogas, two grades of biogas derive passage 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 cleanout fluid, three grades of export mouths 15 of biogas, the primary 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, the inside of described cylindrical container 1 is installed residual particulate matter from low to high successively and is collected container 18, Lower separator 19, Upper separator 20, sludge gas collecting device 21, heat resolve system 22 and dehydrator 23, internally installed the heater 2 of described cylindrical container 1, the top of described heater 2 offers the primary introduction channel 7 of biogas, the lower section of described primary introduction channel 7 is the dehydrator 23 in cylindrical container 1, the primary that lower end is biogas of described heater 2 derives passage 8, the primary of described biogas derives the position of passage 8 above heat resolve 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 radiator 3 including heat pipe, the lower end of the described radiator 3 including heat pipe is installed with two grades of introduction channels 9 of biogas, two grades of introduction channels 9 of biogas are connected with the primary derivation passage 8 of biogas through the primary pipeline 16 of biogas, the upper end of the described radiator 3 including heat pipe is installed with two grades of derivation passages 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 each installed above and below the outer surface of the described radiator 3 including heat pipe, the top and bottom of described water-atomization cooling equipment 4 are respectively mounted the introduction channel 13 of cooling water smoke and the flow pass 14 of cleanout fluid, the outer surface on one side of described water-atomization cooling equipment 4 is provided with three grades of export mouths 15 of biogas.
Described heater 2 is tubular or prism-shaped.
Described heater 2 is installed on the interior surface of cylindrical container 1.
The described radiator 3 including heat pipe can be installed on coiled metal pipes.
Apply such scheme of the present invention, have the advantage that
Substantially reduce the waste liquid of biogas cleaning and the generation of waste gas, may also pass through the generation that structure variation configuration forms methane, make the equipment needs generating content towards biogas of following link, such device form is uncomplicated, expense is not high, biogas constructive system maintainability is good, and can reduce waste liquid and waste gas that biogas cleans.
Accompanying drawing explanation
Fig. 1 is the sectional structure schematic diagram of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, summary of the invention is described further:
With reference to shown in Fig. 1, heater with cavity, described heater is with the cylindrical container 1 of cavity, heater 2, radiator 3 including heat pipe, water-atomization cooling equipment 4, introduction channel 5 for marsh gas raw materials, introduction channel 6 for air, the primary introduction channel 7 of biogas, the primary of biogas derives passage 8, two grades of introduction channels 9 of biogas, two grades of biogas derive passage 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 cleanout fluid, three grades of export mouths 15 of biogas, the primary 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, the inside of described cylindrical container 1 is installed residual particulate matter from low to high successively and is collected container 18, Lower separator 19, Upper separator 20, sludge gas collecting device 21, heat resolve system 22 and dehydrator 23, internally installed the heater 2 of described cylindrical container 1, described heater 2 goes out primary biogas for gathering primary biogas initial gross separation, the top of described heater 2 offers the primary introduction channel 7 of biogas, the lower section of described primary introduction channel 7 is the dehydrator 23 in cylindrical container 1, the primary that lower end is biogas of described heater 2 derives passage 8, the primary of described biogas derives the position of passage 8 above heat resolve 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 radiator 3 including heat pipe, the lower end of the described radiator 3 including heat pipe is installed with two grades of introduction channels 9 of biogas, two grades of introduction channels 9 of biogas are connected with the primary derivation passage 8 of biogas through the primary pipeline 16 of biogas, the upper end of the described radiator 3 including heat pipe is installed with two grades of derivation passages 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 each installed above and below the outer surface of the described radiator 3 including heat pipe, the top and bottom of described water-atomization cooling equipment 4 are respectively mounted the introduction channel 13 of cooling water smoke and the flow pass 14 of cleanout fluid, so cooling liquid just can be sent then through the flow pass 14 of cleanout fluid through water-atomization cooling equipment 4 and repeatedly use, the outer surface on one side of described water-atomization cooling equipment 4 is provided with three grades of export mouths 15 of biogas, so the biogas after cleaning just can pass out to another link.Described heater 2 is tubular or prism-shaped.Described heater 2 is installed on the interior surface of cylindrical container 1.The described radiator 3 including heat pipe can be installed on coiled metal pipes.
When the operation principle of the present invention 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 primary biogas in cylindrical container, the primary introduction channel 7 of biogas leads, primary biogas, the decomposition carried out sulfide and nitride that then heats up into heater 2 after gathering primary biogas, derive passage 8 from the primary of biogas again to derive, the biogas that deriving passage 8 from the primary of biogas derives enters the radiator 3 including heat pipe through the primary pipeline 16 of biogas, after heat pipe cooling, the passage 12 of deriving then through gas discharges the fluid of vaporization, obtain the biogas after cooling, biogas after cooling sends into water-atomization cooling equipment 4 after two grades of derivation passages 10 of biogas flow out, biogas after cleaning flows out through three grades of export mouths 15 of biogas, and cleanout fluid is discharged through the flow pass 14 of cleanout fluid.
By it was verified that with assembly of the invention produce methane content can increase by more than 25%, and often use 500 kilograms of marsh gas raw materials, the content of toxic liquid is reduced to every liter less than 300 milligrams.
The above, it it is only presently preferred embodiments of the present invention, not the present invention is done any pro forma restriction, although the present invention is disclosed above with preferred embodiment, but it is not limited to the present invention, any those skilled in the art, without departing within the scope of technical solution of the present invention, when the technology contents of available the disclosure above makes a little change or is modified to the Equivalent embodiments of equivalent variations, in every case it is without departing from technical solution of the present invention content, technical spirit according to the present invention, within the spirit and principles in the present invention, the any simple amendment that above example is made, equivalent replacement and improvement etc., all still fall within the protection domain of technical solution of the present invention.
Claims (4)
1. the heater with cavity, it is characterized in that the described heater cylindrical container with cavity, heater, radiator including heat pipe, water-atomization cooling equipment, introduction channel for marsh gas raw materials, introduction channel for air, the primary introduction channel of biogas, the primary of biogas derives passage, two grades of introduction channels of biogas, two grades of biogas derive passage, cylindrical container enter aquaporin, the derivation passage of gas, the introduction channel of cooling water smoke, the flow pass of cleanout fluid, three grades of export mouths of biogas, the primary 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, the inside of described cylindrical container 1 is installed residual particulate matter from low to high successively and is collected container, Lower separator, Upper separator, sludge gas collecting device, heat resolve system and dehydrator, internally installed the heater of described cylindrical container, the top of described heater offers the primary introduction channel of biogas, the lower section of described primary introduction channel is the dehydrator in cylindrical container, the primary that the lower end of described heater is biogas derives passage, the primary of described biogas derives the position of passage above heat resolve 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 radiator including heat pipe, the lower end of the described radiator including heat pipe is installed with two grades of introduction channels of biogas, two grades of introduction channels of biogas are connected with the primary derivation passage of biogas through the primary pipeline of biogas, the upper end of the described radiator 3 including heat pipe is installed with two grades of derivation passages 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 each installed above and below the outer surface of the described radiator including heat pipe, the top and bottom of described water-atomization cooling equipment are respectively mounted the introduction channel of cooling water smoke and the flow pass of cleanout fluid, the outer surface on one side of described water-atomization cooling equipment is provided with three grades of export mouths of biogas.
2. the heater with cavity according to claim 1, it is characterised in that described heater is tubular or prism-shaped.
3. the heater with cavity according to claim 1, it is characterised in that described heater is installed on the interior surface of cylindrical container.
4. the heater with cavity according to claim 1, it is characterised in that. the described radiator including heat pipe can be installed on coiled metal pipes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410407462.5A CN105713826A (en) | 2014-08-19 | 2014-08-19 | Heating device with cavity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410407462.5A CN105713826A (en) | 2014-08-19 | 2014-08-19 | Heating device with cavity |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105713826A true CN105713826A (en) | 2016-06-29 |
Family
ID=56145174
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410407462.5A Pending CN105713826A (en) | 2014-08-19 | 2014-08-19 | Heating device with cavity |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105713826A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101570729A (en) * | 2009-06-12 | 2009-11-04 | 霸州市利华燃气储运有限公司 | Integrated process unit for producing methane by utilizing renewable biomass |
| CN201473525U (en) * | 2009-06-12 | 2010-05-19 | 霸州市利华燃气储运有限公司 | Integrated processing device capable of preparing methane by utilizing renewable biomass |
| CN103848464A (en) * | 2014-02-28 | 2014-06-11 | 长沙威保特环保科技有限公司 | Treatment method of low-temperature evaporation high-concentration sewage |
| CN204138658U (en) * | 2014-08-18 | 2015-02-04 | 姚小兵 | With the heating unit of cavity |
-
2014
- 2014-08-19 CN CN201410407462.5A patent/CN105713826A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101570729A (en) * | 2009-06-12 | 2009-11-04 | 霸州市利华燃气储运有限公司 | Integrated process unit for producing methane by utilizing renewable biomass |
| CN201473525U (en) * | 2009-06-12 | 2010-05-19 | 霸州市利华燃气储运有限公司 | Integrated processing device capable of preparing methane by utilizing renewable biomass |
| CN103848464A (en) * | 2014-02-28 | 2014-06-11 | 长沙威保特环保科技有限公司 | Treatment method of low-temperature evaporation high-concentration sewage |
| CN204138658U (en) * | 2014-08-18 | 2015-02-04 | 姚小兵 | With the heating unit of cavity |
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Application publication date: 20160629 |
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