CN202063887U - Alcohol-based synthetic fuel synthesizer - Google Patents
Alcohol-based synthetic fuel synthesizer Download PDFInfo
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- CN202063887U CN202063887U CN201120151061XU CN201120151061U CN202063887U CN 202063887 U CN202063887 U CN 202063887U CN 201120151061X U CN201120151061X U CN 201120151061XU CN 201120151061 U CN201120151061 U CN 201120151061U CN 202063887 U CN202063887 U CN 202063887U
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Abstract
An alcohol-based synthetic fuel synthesizer comprises a fuel synthesis system, a self-circulation mixing system, a synthetic fuel delivery system and a filling system for finished product cylinders. The fuel synthesis system consists of a methyl alcohol material delivery system, a cosolvent material delivery system and C(carbon)-12 material delivery system, outlets of the methyl alcohol material delivery system, the cosolvent material delivery system and the C-12 material delivery system are connected with an inlet of the self-circulation mixing system after being in parallel connection, an outlet of the self-circulation mixing system is connected with the synthetic fuel delivery system, and an outlet of the synthetic fuel delivery system is connected with an inlet of the filling system for finished product cylinders. The alcohol-based synthetic fuel synthesizer has the advantages of simple structure, short processing procedure, online monitoring, high degree of automation in operation and the like, and is free of loss of raw materials in production and free of production or emission of three industrial wastes.
Description
Technical field
The utility model relates to a kind of civilian alcohol radical synthol, and being specifically related to a kind of is main raw material with methyl alcohol, and carbon 12 and solubility promoter are a kind of civilian alcohol radical synthol of auxiliary material synthetic; The utility model has also related to the synthetic reaction device of synthetic this civilian alcohol radical synthol simultaneously, belongs to compound product and technical field of chemical.
Background technology
Methyl alcohol is not only important chemical material, also is the energy of sanitation and hygiene simultaneously.No matter the production technology of methyl alcohol is big equipment of output or the small-sized production equipment that yields poorly in China, and its technology and production unit are all quite ripe, and especially raw material sources are in coal resources, and its sustainability more possesses advantage than petroleum resources.About utilizing the methyl alcohol energy that acts as a fuel, the applicating history in a lot of years has been arranged in China, country has also formulated " alcohol civil fuel " standard, but because the calorific value of methyl alcohol is lower, compare per kilogram methyl alcohol with oil fuel and only be equivalent to, consume the rate of exchange and finally still be higher than alkane fuel with 47% of weight alkane calorific value.In China because region difference, coal production is than higher place, direct application percentage at its methane of civil area is equivalent to slightly height of oil fuel, especially Shanxi Province, methyl alcohol acts as a fuel in direct use, other areas also do not have the advantage on this region, but this using method, be waste virtually, methyl alcohol as basic raw material, is generated other higher products of calorific value the energy, as energy raw material, and then alternative diesel oil, liquefied petroleum gas (LPG) equal energy source raw material, be the significant problem that is related to the national energy Sustainable development, need to be resolved hurrily.
The raw material of light-hydrocarbon gas and Sweet natural gas, liquefied petroleum gas (LPG) belong to the alkanes petroleum products together, methane (CH
4), ethane (C
2H
6) be the major ingredient of Sweet natural gas, propane (C
3H
8), butane (C
4H
10) be the major ingredient of liquefied petroleum gas (LPG), and pentane (C
5H
12), with hexane (C
6H
14) then be the major ingredient of light-hydrocarbon gas.Weather and liquefied petroleum gas (LPG) are gaseous state under the state at normal temperatures and pressures, event is called geseous fuel, and carbonatoms is 5-6 pentane (C
5H
12) and hexane (C
6H
14), be in a liquid state at normal temperatures and pressures, then be called as liquid light hydrocarbon fuel, through equipment for gasification liquid fuel, gasify and by certain ratio and air mixed with physics mode, just can produce combustible gas, supply with use, Here it is our said novel energy-saving environment-friendly energy---light-hydrocarbon gas at the burner that is being transported to the user by the zonule pipe network.
Chinese patent application number: 00109983.3 discloses a kind of artificial synthetic alcohol base fuel, and it is by useless methyl alcohol, light hydrocarbon fuel, and the additive configuration forms, and its proportioning is: useless methyl alcohol 80 ~ 85%, light hydrocarbon fuel C 5-C8 is 12 ~ 15%, additive 5-6%.Characteristics such as it has free from environmental pollution, and stable in properties is safe in utilization, and cost is low.Because what most of raw material adopted is slightly useless methyl alcohol, it can be regarded as a kind of renewable energy resources, and combustion heat value is suitable with kerosene, diesel oil theoretically, and it can be widely used in occasions such as food and drink, family.
Chinese patent application number: 99121436.6 1 kinds of alcohol radical liquid fuels disclose that to contain the composition that carbon, hydrogen and oxygen forms be main liquid carbon-containing fuel technical field.Contain methyl alcohol, gain of heat agent, solubility promoter, booster, sterilizing agent, weight content is respectively: 70-85%, 10-20%, 2-10%, 1-2%, 0.1-0.2%.It can substitute diesel oil fully and be used for the small-sized oil range cooking of diesel range and street restaurant operation.
The utility model content
Technical problem to be solved in the utility model provides a kind of alcohol radical synthol synthesizer, and this production equipment is simple in structure, does not have material loss in the production process, and no three industrial wastes produce and discharging.
To achieve these goals, the utility model is by the following technical solutions:
A kind of alcohol radical synthol synthesizer, it comprises the fuel synthesis system that is made of methanol feedstock delivery system, solubility promoter source material delivery system, carbon twelve source acupoint material delivery system; Comprise that also self-circulation mixes the canned system of system, synthol delivery system, finished product jar; The outlet of methanol feedstock delivery system, solubility promoter source material delivery system and the carbon twelve source acupoint material delivery system back that is connected in parallel is connected with the import that self-circulation mixes system, the outlet that self-circulation mixes system is connected with the import of synthol delivery system, and the outlet of this synthol delivery system is connected with the import of the canned system of finished product jar.
Described methanol feedstock delivery system is linked to each other with ball valve, pipeline, rapid-acting coupling through Y-tube one end by the inlet of methanol pump, opposite side links to each other with the methane feed jar through ball valve, pipeline, stopping valve, the methane pump outlet links to each other with the methanol feedstock jar with ball valve, pipeline, stopping valve through an end of Y-tube, the other end through Y-tube links to each other with synthesis tank with ball valve, under meter, pipeline and stopping valve, thereby constitutes the methanol feedstock delivery system.
Described solubility promoter source material delivery system is linked to each other with ball valve, pipeline, rapid-acting coupling through Y-tube one end by the inlet of solubility promoter pump, the other end links to each other with the solubility promoter head tank through ball valve, pipeline, stopping valve, the solubility promoter pump outlet links to each other with the solubility promoter head tank with ball valve, pipeline, stopping valve through an end of Y-tube, the other end links to each other with synthesis tank through ball valve, under meter, pipeline and stopping valve, thereby constitutes the solubility promoter source material delivery system.
Described carbon twelve source acupoint material delivery system is linked to each other with ball valve, intake pipeline, rapid-acting coupling by inlet threeway one end on pipeline of carbon twelve source acupoint material pump, the other end of threeway links to each other with carbon twelve source acupoint batch can through ball valve, pipeline, stopping valve, the inlet of carbon twelve source acupoint material pump threeway one end on pipeline links to each other with carbon twelve source acupoint batch can with ball valve, pipeline, stopping valve, the other end of threeway links to each other with synthesis tank through pipeline, ball valve, under meter, pipeline and stopping valve, thereby constitutes carbon twelve source acupoint material delivery system.
Described self-circulation mixes system and is linked to each other with synthesis tank through pipeline, stopping valve by the inlet of recycle pump, outlet of circulating pump links to each other with synthesis tank through pipeline, stopping valve, honeycomb hole pipe, this honeycomb hole pipe is arranged in the synthesis tank, mixes system thereby constitute self-circulation.
Described synthol delivery system is linked to each other with synthesis tank through pipeline, stopping valve by the inlet of synthesis tank Send out pump, and outlet links to each other with the finished product jar through pipeline, stopping valve, thereby constitutes the synthol delivery system.
The canned system of described finished product jar is linked to each other with the finished product jar through pipeline, stopping valve by the inlet of synthol Send out pump, one end of outlet Y-tube on pipeline links to each other with pipeline with a minute pressure pipeline, check valve, pipeline, the other end links to each other with the trestle pipeline through under meter, pipeline, ball valve, be separately installed with ball valve and output interface on the trestle pipeline, thereby constitute the canned system of finished product jar.
Described synthesis tank is provided with the manhole of honeycomb hole pipe maintenance.
Because the technical scheme that has adopted the utility model to provide, show according to the data in the textbook: the calorific value 22.7MJ/kg of methyl alcohol, with the coal 1500 yuan of the production cost less thaies of material benzenemethanol, the calorific value of gasoline is 10000cal/kg, and this alcohol radical synthol of the utility model synthetic is adjusted to the optimum matching state at kitchen range air-valve, fuel tap, its calorific value is 9800cal/kg, and calorific value that this product of per kilogram and air mixed gas firing discharge and diesel oil and liquefied petroleum gas (LPG) are suitable substantially.
The beneficial effects of the utility model are: have that simple in structure, technical process is short, characteristics such as on-line monitoring and automated operation degree height, do not have material loss in the production process, no three industrial wastes produce and discharge.
Description of drawings
The alcohol radical synthol synthesizer synoptic diagram that Fig. 1 provides for the utility model.
Embodiment
As shown in Figure 1:
1, described methanol feedstock delivery system is by inlet process Y-tube (81) one ends and the ball valve (6) of methanol pump (1), pipeline (5), rapid-acting coupling (2) links to each other, the other end is through ball valve (9), pipeline (10), stopping valve (13) links to each other with methanol feedstock jar (14), the outlet of methanol pump (1) is through an end and the ball valve (19) of Y-tube (18), pipeline (11), stopping valve (12) links to each other with methanol feedstock jar (14), the other end and ball valve (17) through Y-tube (18), under meter (16), pipeline (15) links to each other with synthesis tank (52) with (59) and stopping valve (47), thereby constitutes the methanol feedstock delivery system.
2, described solubility promoter source material delivery system is linked to each other with solubility promoter head tank (26) with ball valve (21), pipeline (23), stopping valve (25) through Y-tube (80) one ends by the inlet of solubility promoter pump (20), the outlet of solubility promoter pump (20) links to each other with solubility promoter head tank (26) with ball valve (30), pipeline (31), stopping valve (24) through an end of Y-tube (79), the other end links to each other with synthesis tank (52) through ball valve (29), under meter (28), pipeline (27), (59) and stopping valve (47), thereby constitutes the solubility promoter source material delivery system.
3, described carbon twelve source acupoint material delivery system is by inlet threeway (82) one ends and ball valve (33) on pipeline of carbon twelve source acupoint material pump (32), intake pipeline (8), rapid-acting coupling (4) links to each other, the other end of threeway is through ball valve (34), pipeline (38), stopping valve (36) links to each other with carbon twelve source acupoint batch can (37), the inlet of carbon twelve source acupoint material pump (32) is threeway (43) one ends and ball valve (42) on pipeline, pipeline (40), stopping valve (39) links to each other with carbon twelve source acupoint batch can (37), the other end of threeway is through pipeline, ball valve (44), under meter (45), pipeline (46) links to each other with synthesis tank (52) with (59) and stopping valve (47), thereby constitutes carbon twelve source acupoint material delivery system.
4, the described self-circulation system that mixes is linked to each other with synthesis tank (52) through pipeline (57), stopping valve (48) by the inlet of recycle pump (58), the outlet of recycle pump (58) links to each other with synthesis tank (52) with (56), stopping valve (55), honeycomb hole pipe (51) through pipeline (49), this honeycomb hole pipe (51) is arranged in the synthesis tank (52), mixes system thereby constitute self-circulation.
5, described synthol delivery system is linked to each other with synthesis tank (52) through pipeline (54), stopping valve (50) by the inlet of synthesis tank Send out pump (60), outlet links to each other with finished product jar (61) with (69), stopping valve (78) through pipeline (53), thereby constitutes the synthol delivery system.
6, the canned system of described finished product jar is linked to each other with finished product jar (61) through pipeline (73), stopping valve (74) by the inlet of synthol Send out pump (70), one end of outlet Y-tube (71) on pipeline links to each other with pipeline (73) with dividing line ball (76), check valve (75), pipeline (72), and the other end links to each other with trestle pipeline (64) through under meter (77), pipeline (68), ball valve (67); Be separately installed with ball valve (62), (66) and output interface (63), (65) on the trestle pipeline (64), in order to oily car weight dress alcohol radical synthol, thereby constitute the canned system of finished product jar; Manhole (35) on the synthesis tank (52) is the access hole of honeycomb hole pipe (51).
The structural principle of this process unit is summarized as follows:
The methanol feedstock processand:
Close ball valve (9) and ball valve (17), open ball valve (19) and stopping valve (12), rapid-acting coupling (2) is linked to each other with the tank wagon interface, start methanol pump (1), it is standby that methanol feedstock passes through rapid-acting coupling (2), pipeline (5), ball valve (6), Y-tube (81), methanol pump (1), Y-tube (18), ball valve (19), pipeline (11) successively, stopping valve (12) enters methanol feedstock jar (14) storage.
Solubility promoter raw material processand:
Close ball valve (22) and ball valve (29), open ball valve (21) and ball valve (30), stopping valve (24), rapid-acting coupling (3) is linked to each other with the tank wagon interface, start solubility promoter pump (1), it is standby that the solubility promoter raw material passes through rapid-acting coupling (3), pipeline (7), ball valve (21), solubility promoter pump (20), Y-tube (79), ball valve (30), pipeline (31) successively, stopping valve (24) enters solubility promoter head tank (26) storage.
Carbon twelve source acupoint material processand:
Close ball valve (34) and ball valve (44), open ball valve (33) and ball valve (42), stopping valve (39), rapid-acting coupling (4) is linked to each other with the tank wagon interface, start carbon 12 pumps (32), it is standby that carbon twelve source acupoint material passes through rapid-acting coupling (4), pipeline (8), ball valve (33), Y-tube (82), pipeline (41), carbon twelve source acupoint material pump (32), Y-tube (43), ball valve (42), pipeline (40) successively, stopping valve (39) enters carbon twelve source acupoint batch can (37) storage.
Methanol feedstock input synthesis tank technological process:
Close ball valve (6) and ball valve (19) and ball valve (29) and ball valve (44), stopping valve (50).Open stopping valve (13), ball valve (9), ball valve (17), stopping valve (47), start methanol pump (1), the methanol feedstock in the methanol feedstock jar (14) passes through stopping valve (13), pipeline (10), ball valve (9), Y-tube (81), methanol pump (1), Y-tube (18), ball valve (17), under meter (16), pipeline (15) and pipeline (59) successively and stopping valve (47) enters synthesis tank (52); Observe under meter (16), finish the methanol feedstock input according to quantitative proportioning.
Solubility promoter raw material input synthesis tank technological process:
Close ball valve (21) and ball valve (30) and ball valve (17) and ball valve (44), stopping valve (50).Open ball valve (22), ball valve (29), stopping valve (25), stopping valve (47), start solubility promoter pump (20), the solubility promoter raw material in the solubility promoter head tank (26) passes through stopping valve (25), pipeline (23), ball valve (22), Y-tube (80), solubility promoter pump (20), Y-tube (79), pipeline (15) and pipeline (59) successively and stopping valve (47) enters synthesis tank (52); Observe under meter (28), finish the input of solubility promoter raw material according to quantitative proportioning.
Carbon twelve source acupoint material input synthesis tank technological process:
Close ball valve (33) and ball valve (42) and ball valve (29) and ball valve (17), stopping valve (50).Open stopping valve (36), stopping valve (47), ball valve (34), ball valve (44), start carbon 12 pumps (32), the carbon twelve source acupoint material in the carbon twelve source acupoint batch can (37) passes through stopping valve (36), pipeline (38), ball valve (34), Y-tube (82), carbon 12 pumps (32), Y-tube (43), ball valve (44), under meter (45), pipeline (46) and pipeline (59) successively and stopping valve (47) enters synthesis tank (52); Observe under meter (45), finish the input of carbon twelve source acupoint material according to quantitative proportioning.
Alcohol radical synthol synthesis technique:
Three kinds of raw materials are closed stopping valve (47), stopping valve (50) after all ratio adds synthesis tank (52) according to the rules.Open stopping valve (48), stopping valve (55), and start recycle pump (58).Raw material in synthesis tank this moment (52) passes through stopping valve (48) successively, pipeline (57), recycle pump (58), pipeline (49) and pipeline (56), stopping valve (55), enter in the honeycomb hole pipe (51) in the synthesis tank (52), go out to set hundred little liquid column-sprayings in this honeycomb hole pipe (51), in synthesis tank (52), form mutual dissolved power, so move in circles, and make it fully miscible, every batch of recycle pump (58) work 30 minutes just can complete miscibility, close recycle pump (58) this moment, stopping valve (48), stopping valve (55), the alcohol radical synthol is just finished synthesis process.
The alcohol radical synthol is unloaded and storage technology:
Close stopping valve (74), open stopping valve (50), stopping valve (78), and startup synthesis tank Send out pump (60), raw material in synthesis tank this moment (52) passes through stopping valve (50) successively, pipeline (54), synthesis tank Send out pump (60), pipeline (53) and pipeline (69), stopping valve (78), enter in the finished product jar (61) and store, close stopping valve (78) then, open stopping valve (74), ball valve (67) and ball valve (62) and ball valve (66), output interface is connected with tank wagon, start synthol Send out pump (70) then, alcohol radical synthol in finished product jar this moment (61) just passes through stopping valve (74) successively, pipeline (73), synthol Send out pump (70), Y-tube (71) and under meter (77), pipeline (68), ball valve (67), trestle pipeline (64) and ball valve (66) and ball valve (62) are from output interface (63), (65) entering the tank wagon transportation dispatches from the factory.
Claims (8)
1. alcohol radical synthol synthesizer, it is characterized in that: it comprises the fuel synthesis system that is made of methanol feedstock delivery system, solubility promoter source material delivery system, carbon twelve source acupoint material delivery system; Comprise that also self-circulation mixes the canned system of system, synthol delivery system, finished product jar; The outlet of methanol feedstock delivery system, solubility promoter source material delivery system and the carbon twelve source acupoint material delivery system back that is connected in parallel is connected with the import that self-circulation mixes system, the outlet that self-circulation mixes system is connected with the import of synthol delivery system, and the outlet of this synthol delivery system is connected with the import of the canned system of finished product jar.
2. alcohol radical synthol synthesizer according to claim 1, it is characterized in that: described methanol feedstock delivery system is linked to each other with ball valve, pipeline, rapid-acting coupling through Y-tube one end by the inlet of methanol pump, opposite side links to each other with the methane feed jar through ball valve, pipeline, stopping valve, the methane pump outlet links to each other with the methanol feedstock jar with ball valve, pipeline, stopping valve through an end of Y-tube, the other end through Y-tube links to each other with synthesis tank with ball valve, under meter, pipeline and stopping valve, thereby constitutes the methanol feedstock delivery system.
3. alcohol radical synthol synthesizer according to claim 2, it is characterized in that: described solubility promoter source material delivery system is linked to each other with ball valve, pipeline, rapid-acting coupling through Y-tube one end by the inlet of solubility promoter pump, the other end links to each other with the solubility promoter head tank through ball valve, pipeline, stopping valve, the solubility promoter pump outlet links to each other with the solubility promoter head tank with ball valve, pipeline, stopping valve through an end of Y-tube, the other end links to each other with synthesis tank through ball valve, under meter, pipeline and stopping valve, thereby constitutes the solubility promoter source material delivery system.
4. alcohol radical synthol synthesizer according to claim 3, it is characterized in that: described carbon twelve source acupoint material delivery system is by inlet threeway one end and ball valve on pipeline of carbon twelve source acupoint material pump, intake pipeline, rapid-acting coupling links to each other, the other end of threeway is through ball valve, pipeline, stopping valve links to each other with carbon twelve source acupoint batch can, the inlet of the carbon twelve source acupoint material pump threeway one end and ball valve on pipeline, pipeline, stopping valve links to each other with carbon twelve source acupoint batch can, the other end of threeway is through pipeline, ball valve, under meter, pipeline links to each other with synthesis tank with stopping valve, thereby constitutes carbon twelve source acupoint material delivery system.
5. alcohol radical synthol synthesizer according to claim 4, it is characterized in that: described self-circulation mixes system and is linked to each other with synthesis tank through pipeline, stopping valve by the inlet of recycle pump, outlet of circulating pump links to each other with synthesis tank through pipeline, stopping valve, honeycomb hole pipe, this honeycomb hole pipe is arranged in the synthesis tank, mixes system thereby constitute self-circulation.
6. alcohol radical synthol synthesizer according to claim 5, it is characterized in that: described synthol delivery system is linked to each other with synthesis tank through pipeline, stopping valve by the inlet of synthesis tank Send out pump, outlet links to each other with the finished product jar through pipeline, stopping valve, thereby constitutes the synthol delivery system.
7. alcohol radical synthol synthesizer according to claim 6, it is characterized in that: the canned system of described finished product jar is linked to each other with the finished product jar through pipeline, stopping valve by the inlet of synthol Send out pump, one end of outlet Y-tube on pipeline links to each other with pipeline with a minute pressure pipeline, check valve, pipeline, the other end links to each other with the trestle pipeline through under meter, pipeline, ball valve, be separately installed with ball valve and output interface on the trestle pipeline, thereby constitute the canned system of finished product jar.
8. alcohol radical synthol synthesizer according to claim 7 is characterized in that: described synthesis tank is provided with the manhole of honeycomb hole pipe maintenance.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120151061XU CN202063887U (en) | 2011-05-13 | 2011-05-13 | Alcohol-based synthetic fuel synthesizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120151061XU CN202063887U (en) | 2011-05-13 | 2011-05-13 | Alcohol-based synthetic fuel synthesizer |
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| Publication Number | Publication Date |
|---|---|
| CN202063887U true CN202063887U (en) | 2011-12-07 |
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ID=45057756
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120151061XU Expired - Fee Related CN202063887U (en) | 2011-05-13 | 2011-05-13 | Alcohol-based synthetic fuel synthesizer |
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| CN (1) | CN202063887U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797418A (en) * | 2016-05-11 | 2016-07-27 | 广州工程技术职业学院 | Residual liquid circulation method and system in rectifying productive practice |
| CN109181791A (en) * | 2018-10-24 | 2019-01-11 | 宜昌泽洪新能源科技有限公司 | The system of automatic control alcohol radical synthesis technology |
| CN109628172A (en) * | 2019-01-16 | 2019-04-16 | 宁夏拓森环保能源有限公司 | A kind of Environment-friendlyfuel fuel and preparation method thereof |
-
2011
- 2011-05-13 CN CN201120151061XU patent/CN202063887U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797418A (en) * | 2016-05-11 | 2016-07-27 | 广州工程技术职业学院 | Residual liquid circulation method and system in rectifying productive practice |
| CN105797418B (en) * | 2016-05-11 | 2018-01-16 | 广州工程技术职业学院 | A kind of rectifying productivity real training raffinate round-robin method and system |
| CN109181791A (en) * | 2018-10-24 | 2019-01-11 | 宜昌泽洪新能源科技有限公司 | The system of automatic control alcohol radical synthesis technology |
| CN109628172A (en) * | 2019-01-16 | 2019-04-16 | 宁夏拓森环保能源有限公司 | A kind of Environment-friendlyfuel fuel and preparation method thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111207 Termination date: 20140513 |