CN207210349U - A kind of high-efficiency cleaning alcohol fuel oil process units - Google Patents
A kind of high-efficiency cleaning alcohol fuel oil process units Download PDFInfo
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- CN207210349U CN207210349U CN201721561387.3U CN201721561387U CN207210349U CN 207210349 U CN207210349 U CN 207210349U CN 201721561387 U CN201721561387 U CN 201721561387U CN 207210349 U CN207210349 U CN 207210349U
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- additive
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Abstract
The utility model discloses a kind of high-efficiency cleaning alcohol fuel oil process units, there is retort, particularly：Emptying pipeline, main feed mouth and additive A inlet, additive B inlet are provided with the top of the retort, main feed mouth is connected with methanol tank, ethanol storage tank, dimethoxym ethane storage tank, C12 storage tanks, naphtha/condensation oil tank respectively, additive A inlet is connected with No.1 auxiliary material tank, additive B inlet is connected with No. two auxiliary material tanks, the No.1 auxiliary material tank and No. two auxiliary material tanks are provided with discharging opening in bottom, and top is provided with charge door；The charge door of No.1 auxiliary material tank is connected with methanol tank, amyl nitrate storage tank, Hydrogen peroxide storage, dimethyl oxalate storage tank respectively, the charge door of No. two auxiliary material tanks is connected with methanol tank, dimethylbenzene storage tank, acetone storage tank respectively, and ferrocene electronic measurement charging bucket is additionally provided with above No. two auxiliary material tanks；The utility model is simple in construction, and it is precisely convenient to control, and production efficiency is high, safety and environmental protection.
Description
Technical field
Alcohol-based fuel technical field is the utility model is related to, particularly a kind of high-efficiency cleaning alcohol fuel oil process units.
Background technology
At present, petroleum resources growing tension, price is constantly soaring, but the market demand is increasing.It is well known that stone
Oil is non-renewable resources, and the strategic goods and materials of country, but is also largely using bavin in many industrial burners at present
Oil, such as burning oil of the ignition oil in thermal power plant, various boilers etc., cause serious capability and performance overstock problem：
Because being only capable of the small part performance using diesel oil in burner, diesel oil resource is not fully utilized, formed a kind of actual
On the wasting of resources, and diesel oil cost is higher, therefore, research and development one kind can diesel oil substitute, and can meets various burner need
Fuel oil ask, that cost is cheap is very necessary.
Based on the reason for the petroleum resources anxiety, Aalcohols fuel is as a kind of biomass energy, due to its recyclability and cleaning
The feature of environmental protection, by the extensive concern of fuel industry, national governments are directed to the exploitation of alcohol-based fuel at present, with alcohols（Such as first
Alcohol, ethanol, butanol etc.）Material is that main body researches and develops New Alcohol Based fuel as the study hotspot in current industry.
But the alcohol-based fuel for having been developed for coming at present is mainly used for commercial use, rather than it is civilian, its is main
The reason for be that alcohol-based fuel calorific value is too low at present, and dosage is too big, make to have more than is needed at all in many occasions, even if can use, by
In its huge dosage, compare with diesel oil in cost also very nearly the same, additionally burner is transformed, therefore at present
Existing alcohol-based fuel can not open up markets, so as to lose practical value.Therefore, a kind of new high heating value, high cleaning are researched and developed
Civilian alcohol fuel oil turns into urgent problem to be solved in industry, and the production equipment for being equally used for producing alcohol fuel oil also needs
In exploitation.
The content of the invention
The purpose of this utility model seeks to solve current diesel oil resource scarcity, and existing alcohol-based fuel is not suitable for the people
Used with burner, and at present also dedicated for production alcohol-based fuel equipment the problem of, there is provided a kind of high-efficiency cleaning
Alcohol fuel oil process units.
Device used in a kind of preparation method of high-efficiency cleaning alcohol fuel oil of the present utility model, has synthesis under normal pressure
Tank, particularly：Bottom is provided with air flow stirring apparatus in the synthesis under normal pressure tank, and emptying pipeline, master are provided with the top of retort
Charging aperture and additive A inlet, additive B inlet, main feed mouth by pipeline respectively with methanol tank, ethanol storage tank,
Dimethoxym ethane storage tank, flotation agent C12 storage tanks, naphtha/condensation oil tank are connected, and additive A inlet passes through pipeline and No.1
Auxiliary material tank is connected, and additive B inlet is connected by pipeline with No. two auxiliary material tanks, the No.1 auxiliary material tank and No. two auxiliary materials
Tank carries agitating device, and discharging opening is provided with bottom, and top is provided with charge door；The charge door of No.1 auxiliary material tank passes through pipeline
Be connected respectively with methanol tank, amyl nitrate storage tank, Hydrogen peroxide storage, dimethyl oxalate storage tank, No. two auxiliary material tanks plus
Material mouth is connected with methanol tank, dimethylbenzene storage tank, acetone storage tank respectively by pipeline, and two cyclopentadienyls are additionally provided with above No. two auxiliary material tanks
The sub- metered charge bucket of ferroelectricity.
Band pump electronic flowmeter, all band pump electronic flowmeters and two cyclopentadienyls are equipped with described in the utility model on each pipeline
The electronic measurement feeding device of the sub- metered charge bucket of ferroelectricity is connected with main controller controls.
It is equipped with the tank of No.1 auxiliary material described in the utility model and No. two auxiliary material tanks from tank bottom and is drawn out to tank deck backflow
Closed circulation pipeline, electronic circulation pump is housed on circulating line, for aiding in material in No.1 auxiliary material tank and No. two auxiliary material tanks to follow
Ring is well mixed.
Air flow stirring apparatus described in the utility model is an annular pipeline, and annular pipeline passes through the external compression of pipeline
Air reservoir, some solarization air caps arranged obliquely is uniformly offered on annular pipeline, each solarization air cap is in annular pipeline
On deviation angle it is identical, the aperture of the solarization air cap is 3-6mm.
Solarization air cap described in the utility model is 30 ° with the deviation angle of vertical direction on annular pipeline.
A kind of application method of high-efficiency cleaning alcohol fuel oil process units of the present utility model is as follows：
（1）Dimethoxym ethane, flotation agent C12 are added in the synthesis under normal pressure tank with air flow stirring apparatus by formula ratio, opened
Air flow stirring apparatus, stir 15~20 minutes；Again into retort by formula ratio sequentially add ethanol, naphtha or condensate,
The methanol of 1/3 formula ratio, air flow stirring apparatus is opened, stirred 15~20 minutes；
（2）Amyl nitrate, hydrogen peroxide and dimethyl carbonate are added into No.1 auxiliary material tank by formula ratio, then to No.1 auxiliary material
The methanol that 1/3 formula ratio is added in tank is diluted, and stirring must dilute sufficient additive A in 15~20 minutes, then will add
Agent A is added in retort by 20L/h flow velocity, continues stirring 15~20 minutes；
（3）Diesel oil is injected into No. two auxiliary material tanks, then adds into No. two auxiliary material tanks the methanol of 1/3 formula ratio and is diluted,
Dimethylbenzene, ferrocene, acetone are sequentially added into No. two auxiliary material tanks again, stirring must dilute sufficient additive B in 15~20 minutes,
Then additive B is added in retort by 20L/h flow velocity, continues stirring 15~20 minutes, produce high cleaning alcohol fuel
Oil.
The utility model is simple in construction, and it is precisely convenient to control, and production efficiency is high, and main production equipments use normal pressure
Container atmospheric operation, Safety and Environmental Protection are high.The alcohol-based fuel calorific value of production is high, and impurity is few, and combustion efficiency is excellent, clean tail gas,
Safety, it is pollution-free, suitable for electric boiler, plain cylindrical furnace, catering trade and various burners oil, there is high economic benefit
And social benefit.
Brief description of the drawings
Fig. 1 is the main structure diagram of the utility model device；
In figure, 1-retort, 2-air flow stirring apparatus, 3-emptying pipeline, 4-main feed mouth, the injection of 5-additive A
Mouthful, 6-additive B inlet, 7-pipeline, 8-methanol tank, 9-ethanol storage tank, 10-dimethoxym ethane storage tank, 11-C12 storages
Tank, 12-naphtha/condensation oil tank, 13-No.1 auxiliary material tank, 14-No. two auxiliary material tanks, 15-No.1 auxiliary material tank charge door,
16-amyl nitrate storage tank, 17-Hydrogen peroxide storage, 18-dimethyl oxalate storage tank, 19-No. two auxiliary material tank charge doors,
20-dimethylbenzene storage tank, 21-acetone storage tank, 22-ferrocene electronic measurement charging bucket, 23-band pump electronic flowmeter, 24-
Electronic measurement feeding device, 25-master controller, 26-circulating line, 27-electronic circulation pump, 28-annular pipeline, 29-
Compressed air reservoir.
Embodiment
Embodiment 1
Referring to Fig. 1, a kind of high-efficiency cleaning alcohol fuel oil process units of the present embodiment, there is synthesis under normal pressure tank 1, especially
It is：Bottom is provided with air flow stirring apparatus 2 in the synthesis under normal pressure tank 1, and the top of retort 1 is provided with emptying pipeline 3, main feed
Mouthfuls 4 and additive A inlet 5, additive B inlet 6, main feed mouth 4 by pipeline 7 respectively with methanol tank 8, ethanol storage tank
9th, dimethoxym ethane storage tank 10, flotation agent C12 storage tanks 11, naphtha/condensation oil tank 12 are connected, and additive A inlet 5 passes through pipe
Road 7 is connected with No.1 auxiliary material tank 13, and additive B inlet 6 is connected by pipeline 7 with No. two auxiliary material tanks 14, the No.1
Auxiliary material tank 13 and No. two auxiliary material tanks 14 carry agitating device, and discharging opening is provided with bottom, and top is provided with charge door；No.1 is auxiliary
The charge door 15 of batch can by pipeline 7 respectively with methanol tank 8, amyl nitrate storage tank 16, Hydrogen peroxide storage 17, carbonic acid diformazan
Ester storage tank 18 is connected, the charge doors 19 of No. two auxiliary material tanks by pipeline 7 respectively with methanol tank 8, dimethylbenzene storage tank 20, acetone
Storage tank 21 is connected, and No. two tops of auxiliary material tank 14 are additionally provided with ferrocene electronic measurement charging bucket 22.
Be equipped with band pump electronic flowmeter 23 described in the present embodiment on each pipeline 7, all band pump electronic flowmeters 23 and
The electronic measurement feeding device 24 of ferrocene electronic measurement charging bucket 22 is controlled with master controller 25 and connected.
It is equipped with the tank of No.1 auxiliary material described in the present embodiment 13 and No. two auxiliary material tanks 14 from tank bottom and is drawn out to tank deck backflow
Closed circulation pipeline 26, electronic circulation pump 27, auxiliary No.1 auxiliary material tank 13 and No. two auxiliary material tanks 14 are housed on circulating line 26
Interior Matter Transfer is well mixed.
Air flow stirring apparatus 2 described in the present embodiment is an annular pipeline 28, and annular pipeline passes through the external pressure of pipeline
Contracting air reservoir 29, some solarization air caps arranged obliquely is uniformly offered on annular pipeline 28, each solarization air cap 30 is in circle
Deviation angle on circulating line 28 is identical, and the aperture of the solarization air cap is 3-6mm.Solarization air cap is in annulus described in the present embodiment
With the deviation angle of vertical direction it is 30 ° on shape pipeline 28.It is not detailed in figure because such a air flow stirring apparatus is prior art
Show.The air flow stirring apparatus of other structures can also be used in certain the utility model, as long as the utility model can be reached
The demand of middle liquid agitation.
Claims (4)
1. a kind of high-efficiency cleaning alcohol fuel oil process units, there is synthesis under normal pressure tank, it is characterised in that：In the synthesis under normal pressure
Bottom is provided with air flow stirring apparatus in tank, and emptying pipeline, main feed mouth and additive A inlet are provided with the top of retort, is added
Add agent B inlets, main feed mouth by pipeline respectively with methanol tank, ethanol storage tank, dimethoxym ethane storage tank, flotation agent C12 storage tanks,
Naphtha/condensation oil tank is connected, and additive A inlet is connected by pipeline with No.1 auxiliary material tank, additive B inlet
It is connected by pipeline with No. two auxiliary material tanks, the No.1 auxiliary material tank and No. two auxiliary material tanks carry agitating device, and in bottom
Provided with discharging opening, top is provided with charge door；The charge door of No.1 auxiliary material tank is stored up with methanol tank, amyl nitrate respectively by pipeline
Tank, Hydrogen peroxide storage, dimethyl oxalate storage tank are connected, and the charge door of No. two auxiliary material tanks is stored up with methanol respectively by pipeline
Tank, dimethylbenzene storage tank, acetone storage tank are connected, and ferrocene electronic measurement charging bucket is additionally provided with above No. two auxiliary material tanks.
A kind of 2. high-efficiency cleaning alcohol fuel oil process units according to claim 1, it is characterised in that：Each pipeline
On be equipped with band pump electronic flowmeter, it is all with the electronic measurement of pump electronic flowmeter and ferrocene electronic measurement charging bucket feed
Device is connected with main controller controls.
A kind of 3. high-efficiency cleaning alcohol fuel oil process units according to claim 1, it is characterised in that：The No.1 is auxiliary
The closed circulation pipeline that tank deck backflow is drawn out to from tank bottom is equipped with batch can and No. two auxiliary material tanks, electronics is housed on circulating line
Circulating pump, for aiding in Matter Transfer in No.1 auxiliary material tank and No. two auxiliary material tanks to be well mixed.
A kind of 4. high-efficiency cleaning alcohol fuel oil process units according to claim 1, it is characterised in that：The air-flow stirs
It is an annular pipeline to mix device, and annular pipeline is uniformly opened up on annular pipeline by pipeline external compressed air storage tank
There are some solarization air caps arranged obliquely, deviation angle of each solarization air cap on annular pipeline is identical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721561387.3U CN207210349U (en) | 2017-11-21 | 2017-11-21 | A kind of high-efficiency cleaning alcohol fuel oil process units |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721561387.3U CN207210349U (en) | 2017-11-21 | 2017-11-21 | A kind of high-efficiency cleaning alcohol fuel oil process units |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207210349U true CN207210349U (en) | 2018-04-10 |
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ID=61819157
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721561387.3U Expired - Fee Related CN207210349U (en) | 2017-11-21 | 2017-11-21 | A kind of high-efficiency cleaning alcohol fuel oil process units |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207210349U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111773995A (en) * | 2020-07-06 | 2020-10-16 | 中润油新能源股份有限公司 | Intelligent production system applied to alcohol-based fuel blending and additive preparation |
-
2017
- 2017-11-21 CN CN201721561387.3U patent/CN207210349U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111773995A (en) * | 2020-07-06 | 2020-10-16 | 中润油新能源股份有限公司 | Intelligent production system applied to alcohol-based fuel blending and additive preparation |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| 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: 20180410 Termination date: 20191121 |