CN103908918A - Production process of novel fuel and fabrication method of system device for producing novel fuel - Google Patents
Production process of novel fuel and fabrication method of system device for producing novel fuel Download PDFInfo
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- CN103908918A CN103908918A CN201410163724.8A CN201410163724A CN103908918A CN 103908918 A CN103908918 A CN 103908918A CN 201410163724 A CN201410163724 A CN 201410163724A CN 103908918 A CN103908918 A CN 103908918A
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Abstract
The invention discloses a production process of novel fuel and a fabrication method of a system device for producing the novel fuel. First to seventh raw material tanks, first to seventh feeding control valves, and first to seventh electronic flow meters are arranged on the system device; first to third raw material delivery pipes are connected with first to fifth primary material mixing tanks, respectively; fourth to seventh raw material delivery pipes are connected to first and second emulsifying and homogeneous mixing equipment, respectively; eighth to thirty-fifth control valves and eighth to thirty-fifth electronic flow meters are respectively arranged on branch pipes of the raw material delivery pipes; third to seventh emulsifying and homogeneous mixing equipment and thirty-sixth to fortieth control valves are respectively arranged on the raw material delivery pipes at the lower parts of the mixing tanks from the left to the right; a forty-first control valve, a product oil storage tank, a forty-second oil discharge control valve and a gasoline flow meter are arranged on the product oil delivery pipe in the system device. A plurality of feeding holes are formed in the raw material delivery pipes at the right upper part of the system device, and an oil outlet is formed in the product oil storage tank at the lower part of the system device.
Description
Technical field
The present invention relates to production technology and the system equipment of fuel, particularly for the manufacture field of the production technology of fuel production enterprise and the preparation method of system and device thereof.
Background technology
China is a rich coal, oil-poor, there is one of country of gas, along with the fast development of national economy, automobile pollution is also in continuous rising, show according to interrelated data, within 2012, automobile quantity has exceeded 2.4 hundred million (wherein 1.2 hundred million is strong car), expect the year two thousand twenty total vehicle and will reach 3.3 hundred million, the year two thousand thirty will reach hundred million of 4.3-5, as can be seen here, within following 20 years, China will face severe energy problem, if or else change the energy and be overly dependent upon for a long time the situation of natural oil, the ability of energy sustainable development will be seriously undermined, if the too dependence on import oil of fuel for motor vehicle of China, will have influence on the alternative of International Politics field decision-making, therefore, to the searching of oil replacement fuel, the China of rapid economic development is seemed to even more important.
At present, China's oil imbalance between supply and demand day is aobvious outstanding, interdependency to import increases year by year, end in October, 2013, the domestic oil consumption demand of China has broken through 4.5 hundred million tons, will reach 5.14 hundred million tons to the end of the year 2013, expect the year two thousand twenty and will break through 700,000,000 tons, even the highlyest will break through 7.8 hundred million tons, the external interdependency of CNPC constantly expands thus, likely will reach 70% to the year two thousand twenty, but, China's natural gas gross reserves is 38 tcms, coal gross reserves is 1,145 hundred million tons, therefore, apply New-type fuel and be used as supplementing of petroleum resources, China has been had to very important strategic importance.
Now there is on the market the fuel production equipment of many different qualities, but on design and structure, there is certain defect, especially in production technology, in power adjustment, in intelligentized design and in practicality, become a technical bottleneck of this series products, its existing equipment mainly mixing based on to industrial chemicals manufactures and designs, the object that reaches general production designs, and can not solve fuel production enterprise and use this type of production equipment to become the object that object dispersion, emulsification, homogeneous, conveying, deposit and power consumption are little and noise is low.
Summary of the invention
The object of this invention is to provide a kind of production technology of New-type fuel and the preparation method of system and device thereof, in the process that uses system and device, reach the problem that object dispersion, emulsification, homogeneous, conveying, deposit and power consumption are little and noise is low to solve fuel production enterprise.Object of the present invention is realized by following technical scheme: a kind of production technology of New-type fuel and the preparation method of system and device thereof, comprise head tank, blending tank, emulsifying homogeneous mixing plant, product oil storage tank, fuel transfer system, control valve, electronic flowmeter, gasoline flowmeter, is characterized in that: the top of this system and device is from left to right provided with the first feed line and the first head tank and the first charging control valve and the first electronic flowmeter, the second feed line and the second head tank and the second charging control valve and the second electronic flowmeter, the 3rd feed line and the 3rd head tank and the 3rd charging control valve and the 3rd electronic flowmeter, the right of this system and device is provided with the 4th feed line and the 4th head tank and the 4th charging control valve and quadrielectron formula flowmeter from top to down, Wuyuan material conveying tube and the 4th head tank and the 5th charging control valve and the 5th electronic flowmeter, the 6th feed line and the 6th head tank and the 6th charging control valve and the 6th electronic flowmeter, the 7th feed line and the 7th head tank and the 7th charging control valve and the 7th electronic flowmeter, be connected to respectively the first major ingredient blending tank on this first to the 3rd feed line, the second major ingredient blending tank, the 3rd major ingredient blending tank, the 4th major ingredient blending tank, the 5th major ingredient blending tank, is connected to respectively the first emulsifying homogeneous mixing plant and the second emulsifying homogeneous mixing plant on the 4th to the 7th feed line, be respectively arranged with the 8th control valve and the 8th electronic flowmeter on the branched pipe of described the first feed line, the 9th control valve and the 9th electronic flowmeter, the tenth control valve and the tenth electronic flowmeter, the 11 control valve and the 11 electronic flowmeter, the 12 control valve and the 12 electronic flowmeter, be respectively arranged with the 13 control valve and the 13 electronic flowmeter on the branched pipe of described the second feed line, the 14 control valve and the tenth quadrielectron formula flowmeter, the 15 control valve and the 15 electronic flowmeter, the 16 control valve and the 16 electronic flowmeter, the 17 control valve and the 17 electronic flowmeter, be respectively arranged with the 18 control valve and the 18 electronic flowmeter on the branched pipe of described the 3rd feed line, the 19 control valve and the 19 electronic flowmeter, the 20 control valve and the 20 electronic flowmeter, the 21 control valve and the 21 electronic flowmeter, the 22 control valve and the 22 electronic flowmeter, be respectively arranged with the 23 control valve and the 23 electronic flowmeter on the branched pipe of described the 4th feed line, the 24 control valve and the 20 quadrielectron formula flowmeter, be respectively arranged with the 25 control valve and the 25 electronic flowmeter on the branched pipe of described Wuyuan material conveying tube, the 26 control valve and the 26 electronic flowmeter, be respectively arranged with the 27 control valve and the 27 electronic flowmeter on the branched pipe of described the 6th feed line, the 28 control valve and the 28 electronic flowmeter, be respectively arranged with the 29 control valve and the 29 electronic flowmeter on the branched pipe of described the 7th feed line, the 30 control valve and the 30 electronic flowmeter, the 31 control valve and the 31 electronic flowmeter, the 32 control valve and the 32 electronic flowmeter, the 33 control valve and the 33 electronic flowmeter, the 34 control valve and the 30 quadrielectron formula flowmeter, the 35 control valve and the 35 electronic flowmeter, be from left to right respectively arranged with the 3rd emulsifying homogeneous mixing plant on the feed line of described blending tank bottom, the 4th emulsifying homogeneous mixing plant, the 5th emulsifying homogeneous mixing plant, the 6th emulsifying homogeneous mixing plant and the 7th emulsifying homogeneous mixing plant and the 36 control valve, the 37 control valve, the 38 control valve, the 39 control valve and the 40 control valve, on product oil carrier pipe in this system and device, be provided with the 41 control valve and product oil storage tank and the 42 goes out oil control valve and gasoline flowmeter, on the feed line of this system and device upper right quarter, be provided with multiple charging apertures, on the product oil storage tank of system and device bottom, have oil-out.
In above-mentioned design, the present invention adopts this system and device, needs with the difference using for fuel production enterprise.As fuel production enterprise is needed to the storage of raw materials, transferring raw material, be uniformly mixed raw material, POL measuring and product oil store, the present invention enables native system device to it and produces processing.
Compared with prior art (on the basis of existing production technology), the present invention is directed to existing production technology, increased the settings such as head tank, blending tank, emulsifying homogeneous mixing plant, product oil storage tank, fuel transfer system, control valve, electronic flowmeter, gasoline flowmeter.In the present invention, head tank is the various liquid raw materials of splendid attire effectively, so that stand-by, blending tank can effectively mix the various liquid raw materials of splendid attire, makes object reach preliminary mixing, dispersion, emulsification, homogeneous, emulsifying homogeneous mixing plant can make object dispersion, emulsification, homogeneous effectively again, and the advantage such as the little and noise of tool power consumption is low, meanwhile, can be according to liquid homogenizing situation, select one-level power, second motive force, three grades of power and timing setting, electronic flowmeter can effectively quantitatively add various raw material, make raw-material quantity and production time by computer software control, the operation principle of its electromagnetic flowmeter is based on Faraday's electromagnetic induction law, in electromagnetic flowmeter, conducting medium in measuring tube is equivalent to the conducting metal bar in faraday's test, two solenoids at upper and lower two ends produce stationary magnetic field, in the time having conducting medium to flow through, can produce induced voltage, the induced voltage that two electrode measurements of pipe interior produce, measuring channel is by nonconducting liner (rubber, teflon etc.) electromagnetic isolation of realization and fluid and measurement electrode, various pipelines, control valve and electronic flowmeter in fuel transfer system can effectively be controlled the output of raw-material input and product oil, gasoline flowmeter, product oil storage tank be the various product oils of splendid attire effectively, have the low viscous medium of measurement (as: water, diesel oil, gasoline etc.), can effectively measure flow and the total amount of liquid, this Technological Economy practicality, safe and reliable, high, the production technology of design level significantly, can effectively meet user's demand.
The present invention has following features: 1, effective various liquid raw materials of splendid attire, so that stand-by.2, can effectively mix the various liquid raw materials of splendid attire, make object reach preliminary mixing, dispersion, emulsification, homogeneous.3, can effectively again make object dispersion, emulsification, homogeneous, and the advantage such as the little and noise of tool power consumption is low, meanwhile, can be according to liquid homogenizing situation, select one-level power, second motive force, three grades of power and timing setting.4, can effectively quantitatively add various raw material, make raw-material quantity and production time by computer software control, the operation principle of its electromagnetic flowmeter is based on Faraday's electromagnetic induction law, in electromagnetic flowmeter, conducting medium in measuring tube is equivalent to the conducting metal bar in faraday's test, two solenoids at upper and lower two ends produce stationary magnetic field, in the time having conducting medium to flow through, can produce induced voltage, the induced voltage that two electrode measurements of pipe interior produce, measuring channel is by nonconducting liner (rubber, teflon etc.) electromagnetic isolation of realization and fluid and measurement electrode.5, can effectively control the output of raw-material input and product oil.6, effective various product oils of splendid attire, and tool measures low viscous medium (as: water, diesel oil, gasoline etc.), can effectively measure flow and the total amount of liquid.7, this Technological Economy practicality, safe and reliable, high, the production technology of design level significantly, can effectively meet user's demand.
The present invention is economic and practical, safe and reliable, high, the production technology of design level significantly, be particularly suitable for fuel, dyestuff and drink enterprise and use.
Brief description of the drawings
below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation:
fig. 1 is the device connection diagram of one embodiment of the invention;
fig. 2 is the production technological process of native system device.
Detailed description of the invention
Fig. 1 illustrates the situation of system and device of the present invention, as used for fuel production enterprise, first by feed line, the raw material in head tank 1 and 2 is prepared enough, open all corresponding control valves 8 and electronic flowmeter 9 simultaneously, and then raw material is entered in corresponding emulsifying homogeneous mixing plant 3 and blending tank 4 and emulsifying homogeneous mixing plant 5, carry out the processing such as elementary object dispersion, emulsification, homogeneous to termination, homogeneous finished oil after treatment through control valve 6 be sent in product oil storage tank 7 for.
In Fig. 2, system and device is by head tank a, blending tank b, emulsifying homogeneous mixing plant c, product oil storage tank d and fuel transfer system e composition, head tank a, blending tank b, emulsifying homogeneous mixing plant c, product oil storage tank d and fuel transfer system e are formed by connecting by pipe network, the top of this system and device is from left to right provided with the first feed line and the first head tank 1 and the first charging control valve 21 and the first electronic flowmeter 22, the second feed line and the second head tank 2 and the second charging control valve 23 and the second electronic flowmeter 24, the 3rd feed line and the 3rd head tank 3 and the 3rd charging control valve 25 and the 3rd electronic flowmeter 26, the right of this system and device is provided with the 4th feed line and the 4th head tank 4 and the 4th charging control valve 27 and quadrielectron formula flowmeter 28 from top to down, Wuyuan material conveying tube and the 4th head tank 5 and the 5th charging control valve 29 and the 5th electronic flowmeter 30, the 6th feed line and the 6th head tank 6 and the 6th charging control valve 31 and the 6th electronic flowmeter 32, the 7th feed line and the 7th head tank 7 and the 7th charging control valve 33 and the 7th electronic flowmeter 34, on this first to the 3rd feed line, be connected to respectively the first major ingredient blending tank 8, the second major ingredient blending tank 9, the 3rd major ingredient blending tank 10, the 4th major ingredient blending tank 11, the 5th major ingredient blending tank 12, on the 4th to the 7th feed line, be connected to respectively the first emulsifying homogeneous mixing plant 13 and the second emulsifying homogeneous mixing plant 14, on the branched pipe of described the first feed line, be respectively arranged with the 8th control valve 36 and the 8th electronic flowmeter 37, the 9th control valve 38 and the 9th electronic flowmeter 39, the tenth control valve 40 and the tenth electronic flowmeter 41, the 11 control valve the 42 and the 11 electronic flowmeter 43, the 12 control valve the 44 and the 12 electronic flowmeter 45, on the branched pipe of described the second feed line, be respectively arranged with the 13 control valve the 46 and the 13 electronic flowmeter 47, the 14 control valve 48 and the tenth quadrielectron formula flowmeter 49, the 15 control valve the 50 and the 15 electronic flowmeter 51, the 16 control valve the 52 and the 16 electronic flowmeter 53, the 17 control valve the 54 and the 17 electronic flowmeter 55, on the branched pipe of described the 3rd feed line, be respectively arranged with the 18 control valve the 56 and the 18 electronic flowmeter 57, the 19 control valve the 58 and the 19 electronic flowmeter 59, the 20 control valve the 60 and the 20 electronic flowmeter 61, the 21 control valve the 62 and the 21 electronic flowmeter 63, the 22 control valve the 64 and the 22 electronic flowmeter 65, on the branched pipe of described the 4th feed line, be respectively arranged with the 23 control valve the 66 and the 23 electronic flowmeter 67, the 24 control valve the 68 and the 20 quadrielectron formula flowmeter 69, on the branched pipe of described Wuyuan material conveying tube, be respectively arranged with the 25 control valve the 70 and the 25 electronic flowmeter 71, the 26 control valve the 72 and the 26 electronic flowmeter 73, on the branched pipe of described the 6th feed line, be respectively arranged with the 27 control valve the 74 and the 27 electronic flowmeter 75, the 28 control valve the 76 and the 28 electronic flowmeter 77, on the branched pipe of described the 7th feed line, be respectively arranged with the 29 control valve the 78 and the 29 electronic flowmeter 79, the 30 control valve the 80 and the 30 electronic flowmeter 81, the 31 control valve the 82 and the 31 electronic flowmeter 83, the 32 control valve the 84 and the 32 electronic flowmeter 85, the 33 control valve the 86 and the 33 electronic flowmeter 87, the 34 control valve the 88 and the 30 quadrielectron formula flowmeter 89, the 35 control valve the 90 and the 35 electronic flowmeter 91, on the feed line of described blending tank bottom, be from left to right respectively arranged with the 3rd emulsifying homogeneous mixing plant 15, the 4th emulsifying homogeneous mixing plant 16, the 5th emulsifying homogeneous mixing plant 17, the 6th emulsifying homogeneous mixing plant 18 and the 7th emulsifying homogeneous mixing plant the 19 and the 36 control valve 92, the 37 control valve 93, the 38 control valve 94, the 39 control valve the 95 and the 40 control valve 96, on product oil carrier pipe in this system and device, be provided with the 41 control valve 97 and product oil storage tank the 20 and the 42 goes out oil control valve 98 and gasoline flowmeter 99, on the feed line of this system and device upper right quarter, be provided with multiple charging aperture f, on the product oil storage tank of system and device bottom, have oil-out g, the specification of above-mentioned raw materials tank is: height 10000mm × diameter 20000mm, the specification of blending tank is: height 4480mm × diameter 3028mm, the specification of emulsifying homogeneous mixing plant is: height 4480mm × diameter 3028mm, the specification of product oil storage tank is: diameter 10000mm × height 20000mm.
In addition, the blending tank in the present invention and head tank and product oil storage tank can adopt carbon steel material, and various pipelines can adopt stainless steel, to meet quality requirement.
Claims (3)
1. the production technology of a New-type fuel and the preparation method of system and device thereof, comprise head tank, blending tank, emulsifying homogeneous mixing plant, product oil storage tank, fuel transfer system, control valve, electronic flowmeter, gasoline flowmeter, it is characterized in that: the top of this system and device is from left to right provided with the first feed line and the first head tank (1) and the first charging control valve (21) and the first electronic flowmeter (22), the second feed line and the second head tank (2) and the second charging control valve (23) and the second electronic flowmeter (24), the 3rd feed line and the 3rd head tank (3) and the 3rd charging control valve (25) and the 3rd electronic flowmeter (26), the right of this system and device is provided with the 4th feed line and the 4th head tank (4) and the 4th charging control valve (27) and quadrielectron formula flowmeter (28) from top to down, Wuyuan material conveying tube and the 4th head tank (5) and the 5th charging control valve (29) and the 5th electronic flowmeter (30), the 6th feed line and the 6th head tank (6) and the 6th charging control valve (31) and the 6th electronic flowmeter (32), the 7th feed line and the 7th head tank (7) and the 7th charging control valve (33) and the 7th electronic flowmeter (34), on this first to the 3rd feed line, be connected to respectively the first major ingredient blending tank (8), the second major ingredient blending tank (9), the 3rd major ingredient blending tank (10), the 4th major ingredient blending tank (11), the 5th major ingredient blending tank (12), on the 4th to the 7th feed line, be connected to respectively the first emulsifying homogeneous mixing plant (13) and the second emulsifying homogeneous mixing plant (14), on the branched pipe of described the first feed line, be respectively arranged with the 8th control valve (36) and the 8th electronic flowmeter (37), the 9th control valve (38) and the 9th electronic flowmeter (39), the tenth control valve (40) and the tenth electronic flowmeter (41), the 11 control valve (42) and the 11 electronic flowmeter (43), the 12 control valve (44) and the 12 electronic flowmeter (45), on the branched pipe of described the second feed line, be respectively arranged with the 13 control valve (46) and the 13 electronic flowmeter (47), the 14 control valve (48) and the tenth quadrielectron formula flowmeter (49), the 15 control valve (50) and the 15 electronic flowmeter (51), the 16 control valve (52) and the 16 electronic flowmeter (53), the 17 control valve (54) and the 17 electronic flowmeter (55), on the branched pipe of described the 3rd feed line, be respectively arranged with the 18 control valve (56) and the 18 electronic flowmeter (57), the 19 control valve (58) and the 19 electronic flowmeter (59), the 20 control valve (60) and the 20 electronic flowmeter (61), the 21 control valve (62) and the 21 electronic flowmeter (63), the 22 control valve (64) and the 22 electronic flowmeter (65), on the branched pipe of described the 4th feed line, be respectively arranged with the 23 control valve (66) and the 23 electronic flowmeter (67), the 24 control valve (68) and the 20 quadrielectron formula flowmeter (69), on the branched pipe of described Wuyuan material conveying tube, be respectively arranged with the 25 control valve (70) and the 25 electronic flowmeter (71), the 26 control valve (72) and the 26 electronic flowmeter (73), on the branched pipe of described the 6th feed line, be respectively arranged with the 27 control valve (74) and the 27 electronic flowmeter (75), the 28 control valve (76) and the 28 electronic flowmeter (77), on the branched pipe of described the 7th feed line, be respectively arranged with the 29 control valve (78) and the 29 electronic flowmeter (79), the 30 control valve (80) and the 30 electronic flowmeter (81), the 31 control valve (82) and the 31 electronic flowmeter (83), the 32 control valve (84) and the 32 electronic flowmeter (85), the 33 control valve (86) and the 33 electronic flowmeter (87), the 34 control valve (88) and the 30 quadrielectron formula flowmeter (89), the 35 control valve (90) and the 35 electronic flowmeter (91), on the feed line of described blending tank bottom, be from left to right respectively arranged with the 3rd emulsifying homogeneous mixing plant (15), the 4th emulsifying homogeneous mixing plant (16), the 5th emulsifying homogeneous mixing plant (17), the 6th emulsifying homogeneous mixing plant (18) and the 7th emulsifying homogeneous mixing plant (19) and the 36 control valve (92), the 37 control valve (93), the 38 control valve (94), the 39 control valve (95) and the 40 control valve (96), on product oil carrier pipe in this system and device, be provided with the 41 control valve (97) and product oil storage tank (20) and the 42 goes out oil control valve (98) and gasoline flowmeter (99), on the feed line of this system and device upper right quarter, be provided with multiple charging apertures (f), on the product oil storage tank of system and device bottom, have oil-out (g).
2. system and device according to claim 1, it is characterized in that, the specification of the head tank in described system and device is: height 10000mm × diameter 20000mm, the specification of blending tank is: height 4480mm × diameter 3028mm, the specification of emulsifying homogeneous mixing plant is: height 4480mm × diameter 3028mm, the specification of product oil storage tank is: diameter 10000mm × height 20000mm.
3. system and device according to claim 2, is characterized in that, described system and device is formed by connecting by pipe network by head tank, blending tank, emulsifying homogeneous mixing plant, product oil storage tank and fuel transfer system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410163724.8A CN103908918A (en) | 2014-04-23 | 2014-04-23 | Production process of novel fuel and fabrication method of system device for producing novel fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410163724.8A CN103908918A (en) | 2014-04-23 | 2014-04-23 | Production process of novel fuel and fabrication method of system device for producing novel fuel |
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| Publication Number | Publication Date |
|---|---|
| CN103908918A true CN103908918A (en) | 2014-07-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410163724.8A Pending CN103908918A (en) | 2014-04-23 | 2014-04-23 | Production process of novel fuel and fabrication method of system device for producing novel fuel |
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| CN201454476U (en) * | 2009-05-07 | 2010-05-12 | 杭州桐庐洪风新技术新燃料开发有限公司 | Automatic continuous-type production equipment for emulsifying fuel oil |
| CN102527269A (en) * | 2012-02-16 | 2012-07-04 | 广州立白企业集团有限公司 | Continuous production process and equipment for liquid detergent |
| CN102580604A (en) * | 2012-02-29 | 2012-07-18 | 上海鑫赛孚能源科技有限公司 | Alcohol ether fuel syncretizing device and production process for preparing alcohol ether fuels |
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2014
- 2014-04-23 CN CN201410163724.8A patent/CN103908918A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1694946A (en) * | 2002-10-16 | 2005-11-09 | 朴吉远 | Apparatus for producing water-in-oil emulsified fuel and supplying the same |
| US20060143978A1 (en) * | 2002-10-16 | 2006-07-06 | Suk-Ha Hwang | Apparatus for producing water-in-oil emulsifield fuel and supplying the same |
| CN101559339A (en) * | 2009-05-07 | 2009-10-21 | 杭州桐庐洪风新技术新燃料开发有限公司 | Fuel emulsification continuous type automatic production device and fuel emulsification method |
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Application publication date: 20140709 |