CN205222682U - Combustible gas generating device - Google Patents
Combustible gas generating device Download PDFInfo
- Publication number
- CN205222682U CN205222682U CN201521035845.0U CN201521035845U CN205222682U CN 205222682 U CN205222682 U CN 205222682U CN 201521035845 U CN201521035845 U CN 201521035845U CN 205222682 U CN205222682 U CN 205222682U
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- CN
- China
- Prior art keywords
- heat exchanger
- raw material
- combustible gas
- transport pipe
- reformer
- 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.)
- Withdrawn - After Issue
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Abstract
The utility model provides a combustible gas generating device, including the head tank, it is continuous with one -level heat exchanger's feed inlet that the head tank passes through raw materials input tube taoist scriptures feedstock pump, the feed inlet that one -level heat exchanger's silo outlet passes through raw materials input pipeline and second grade heat exchanger links to each other, the feed inlet that second grade heat exchanger's silo outlet passes through raw materials input pipeline and reformer links to each other, the feed inlet that the silo outlet of reformer passes through raw materials input pipeline and methyl alcohol reactor links to each other, the combustible gas export of methyl alcohol reactor links to each other with second grade heat exchanger's bottom through combustible gas pipeline, the bottom that combustible gas pipeline and one -level heat exchanger are passed through to second grade heat exchanger's top links to each other. Its simple structure, low in manufacturing cost, self operation power consumption is low, can add moisture 50 percent -85 percent, methyl alcohol 15 percent -50 percent's mixed liquid thermogenesis hydrogen (content is more than 75 percent), oxygen, carbon monoxide, methane etc. And mix combustible gas, and a large amount of energy are practiced thrift, greatly reduced use cost to the natural gas that the fungible had now.
Description
Technical field:
The utility model relates to a kind of combustible gas generating device.
Background technology:
At present, the combustion gas that people family uses generally is Sweet natural gas, and present Sweet natural gas is general, and all from natural-gas field, belong to Nonrenewable energy resources, use cost is higher, does not also meet the requirement of national energy-saving consumption reduction.And methyl alcohol belongs to renewable resources, methanol plus water forms the low basic cleaning raw material of alcoholic degree, react under 200-260 DEG C of temperature condition, the mixed combustible gas body such as hydrogen (content more than 75%), oxygen, carbon monoxide, methane can be produced, and can not obnoxious flavour be produced after burning, also do not utilize now the device of this characteristic generation inflammable gas.
Utility model content:
The utility model is in order to make up the deficiencies in the prior art, provide a kind of combustible gas generating device, its structure is simple, low cost of manufacture, self-operating power consumption is low, the mixed solution of moisture 50%-85%, methyl alcohol 15%-50% can be added the mixed combustible gas body such as thermogenesis hydrogen (content more than 75%), oxygen, carbon monoxide, methane, alternative existing Sweet natural gas, save mass energy, greatly reduce use cost, solve problems of the prior art.
The utility model for solving the problems of the technologies described above adopted technical scheme is:
A kind of combustible gas generating device, comprise head tank, head tank is connected through the feed(raw material)inlet of feedstock pump with one-level heat exchanger by raw material input channel, the material outlet of one-level heat exchanger is connected with the feed(raw material)inlet of two-stage heat exchanger by raw material input channel, the material outlet of two-stage heat exchanger is connected with the feed(raw material)inlet of reformer by raw material input channel, the material outlet of reformer is connected with the feed(raw material)inlet of methanol reactor by raw material input channel, the inflammable gas outlet of methanol reactor is connected with the bottom of two-stage heat exchanger by inflammable gas transport pipe, the top of two-stage heat exchanger is connected with the bottom of one-level heat exchanger by inflammable gas transport pipe, the top of one-level heat exchanger is connected with supply station by inflammable gas transport pipe, supply station is connected with user side by inflammable gas transport pipe, the thermal oil entrance of methanol reactor is connected with the oil outlet of heat-conducting oil furnace through oil pump by thermal oil transport pipe, the thermal oil outlet of methanol reactor is connected with the thermal oil entrance of reformer by thermal oil transport pipe, and the thermal oil outlet of reformer is connected with the oil return opening of heat-conducting oil furnace by thermal oil transport pipe.
The utility model adopts such scheme, structure is simple, low cost of manufacture, the mixed solution of moisture 50%-85%, methyl alcohol 15%-50% can be added the mixed combustible gas body such as thermogenesis hydrogen (content more than 75%), oxygen, carbon monoxide, methane, alternative existing Sweet natural gas, save mass energy, greatly reduce use cost, meet the requirement of national energy-saving consumption reduction.
Accompanying drawing illustrates:
Fig. 1 is structural representation of the present utility model.
In figure, 1, head tank, 2, raw material input channel, 3, feedstock pump, 4, one-level heat exchanger, 5, two-stage heat exchanger, 6, reformer, 7, methanol reactor, 8, inflammable gas transport pipe, 9, supply station, 10, user side, 11, thermal oil transport pipe, 12, oil pump, 13, heat-conducting oil furnace.
Embodiment:
For clearly demonstrating the technical characterstic of this programme, below by embodiment, and in conjunction with its accompanying drawing, the utility model is elaborated.
As shown in Figure 1, a kind of combustible gas generating device, comprise head tank 1, head tank 1 is connected through the feed(raw material)inlet of feedstock pump 3 with one-level heat exchanger 4 by raw material input channel 2, the material outlet of one-level heat exchanger 4 is connected with the feed(raw material)inlet of two-stage heat exchanger 5 by raw material input channel 2, the material outlet of two-stage heat exchanger 5 is connected with the feed(raw material)inlet of reformer 6 by raw material input channel 2, the material outlet of reformer 6 is connected with the feed(raw material)inlet of methanol reactor 7 by raw material input channel 2, the inflammable gas outlet of methanol reactor 7 is connected by the bottom of inflammable gas transport pipe 8 with two-stage heat exchanger 5, the top of two-stage heat exchanger 5 is connected with the bottom of one-level heat exchanger 4 by inflammable gas transport pipe 8, the top of one-level heat exchanger 4 is connected with supply station 9 by inflammable gas transport pipe 8, supply station 9 is connected with user side 10 by inflammable gas transport pipe 8, the thermal oil entrance of methanol reactor 7 is connected through the oil outlet of oil pump 12 with heat-conducting oil furnace 13 by thermal oil transport pipe 11, the thermal oil outlet of methanol reactor 7 is connected with the thermal oil entrance of reformer 6 by thermal oil transport pipe 11, and the thermal oil outlet of reformer 6 is connected by the oil return opening of thermal oil transport pipe 11 with heat-conducting oil furnace 13.
During work, moisture 50%-85% is loaded with in head tank 1, the mixed solution of methyl alcohol 15%-50%, mixeding liquid temperature is 20 DEG C, through raw material input channel 2, above-mentioned mixed solution is pumped in one-level heat exchanger 4 by feedstock pump 3, then two-stage heat exchanger 5 is entered through raw material input channel 2, reformer 6 is entered again through raw material input channel 2, methanol reactor 7 is entered finally by raw material input channel 2, thermal oil in heat-conducting oil furnace 13 can be delivered to methanol reactor 7 and reformer 6 through thermal oil transport pipe 11 by oil pump 12, after respectively methanol reactor 7 and reformer 6 being heated, thermal oil is back in heat-conducting oil furnace 13 through thermal oil transport pipe 11 again, formation thermal oil circulates.Mixed solution in methanol reactor 7 reacts under 200-260 DEG C of temperature condition, produce hydrogen (content more than 75%), oxygen, carbon monoxide, the mixed combustible gas bodies such as methane, mixed combustible gas temperature is about 240 DEG C, the mixed combustible gas body of 240 DEG C through inflammable gas transport pipe 8 by entering in two-stage heat exchanger 5 bottom two-stage heat exchanger 5, discharged by two-stage heat exchanger 5 top enters in one-level heat exchanger 4 through inflammable gas transport pipe 8 bottom one-level heat exchanger 4 again, discharged by one-level heat exchanger 4 top again and be delivered to supply station 9 through inflammable gas transport pipe 8, finally be delivered to user side 10 by supply station 9 to use.In one-level heat exchanger 4, high temperature mixed combustible gas body and raw material mixed solution carry out heat exchange, raw material mixed solution can be heated to 60 DEG C from 20 DEG C, in two-stage heat exchanger 5, high temperature mixed combustible gas body and raw material mixed solution carry out heat exchange, raw material mixed solution can be heated to 180 DEG C from 60 DEG C, the raw material mixed solution of 180 DEG C in reformer 6 by heat-conducting oil heating to nearly 240 DEG C, then enter methanol reactor 7.And temperature is reduced to 30 DEG C and is entered supply station 9 after 240 DEG C of high temperature mixed combustible gas bodies of twice heat exchange are discharged from one-level heat exchanger 4.By above-mentioned heat exchange circulation process, the power consumption of the utility model self-operating is extremely low, the high temperature mixed combustible gas body produced is utilized to carry out two-stage pre-heating temperature elevation to raw material mixed solution, high temperature mixed combustible gas body is lowered the temperature simultaneously, achieve the cycling and reutilization of heat, save mass energy.The mixed combustible gas body such as hydrogen (content more than 75%), oxygen, carbon monoxide, methane finally produced, alternative existing Sweet natural gas is for household use, saves mass energy, greatly reduces use cost, be suitable for extensively promoting the use of.
Above-mentioned embodiment can not as the restriction to the utility model protection domain, and for those skilled in the art, any alternate modification make the utility model embodiment or conversion all drop in protection domain of the present utility model.
The utility model does not describe part in detail, is the known technology of those skilled in the art of the present technique.
Claims (1)
1. a combustible gas generating device, it is characterized in that: comprise head tank, head tank is connected through the feed(raw material)inlet of feedstock pump with one-level heat exchanger by raw material input channel, the material outlet of one-level heat exchanger is connected with the feed(raw material)inlet of two-stage heat exchanger by raw material input channel, the material outlet of two-stage heat exchanger is connected with the feed(raw material)inlet of reformer by raw material input channel, the material outlet of reformer is connected with the feed(raw material)inlet of methanol reactor by raw material input channel, the inflammable gas outlet of methanol reactor is connected with the bottom of two-stage heat exchanger by inflammable gas transport pipe, the top of two-stage heat exchanger is connected with the bottom of one-level heat exchanger by inflammable gas transport pipe, the top of one-level heat exchanger is connected with supply station by inflammable gas transport pipe, supply station is connected with user side by inflammable gas transport pipe, the thermal oil entrance of methanol reactor is connected with the oil outlet of heat-conducting oil furnace through oil pump by thermal oil transport pipe, the thermal oil outlet of methanol reactor is connected with the thermal oil entrance of reformer by thermal oil transport pipe, and the thermal oil outlet of reformer is connected with the oil return opening of heat-conducting oil furnace by thermal oil transport pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521035845.0U CN205222682U (en) | 2015-12-10 | 2015-12-10 | Combustible gas generating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521035845.0U CN205222682U (en) | 2015-12-10 | 2015-12-10 | Combustible gas generating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205222682U true CN205222682U (en) | 2016-05-11 |
Family
ID=55897759
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521035845.0U Withdrawn - After Issue CN205222682U (en) | 2015-12-10 | 2015-12-10 | Combustible gas generating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205222682U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105347301A (en) * | 2015-12-10 | 2016-02-24 | 刘建安 | Combustible gas generator |
-
2015
- 2015-12-10 CN CN201521035845.0U patent/CN205222682U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105347301A (en) * | 2015-12-10 | 2016-02-24 | 刘建安 | Combustible gas generator |
| CN105347301B (en) * | 2015-12-10 | 2018-01-05 | 刘建安 | A kind of combustible gas generating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160511 Effective date of abandoning: 20180105 |
|
| AV01 | Patent right actively abandoned |