CN106520219B - A kind of High-octane mogas and preparation method thereof - Google Patents
A kind of High-octane mogas and preparation method thereof Download PDFInfo
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- CN106520219B CN106520219B CN201510585161.6A CN201510585161A CN106520219B CN 106520219 B CN106520219 B CN 106520219B CN 201510585161 A CN201510585161 A CN 201510585161A CN 106520219 B CN106520219 B CN 106520219B
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Abstract
Isopentane reconciliation High-octane mogas and preparation method thereof is utilized the invention discloses a kind of, under normal temperature and pressure conditions, by the isopentane of 5%~15% parts by weight, the S_ZORB treated gasoline of 40%~45% parts by weight, the high pressure heavy naphtha of 8%~9% parts by weight, the methyl tertiary butyl ether(MTBE) of 4%~5% parts by weight, the light raffinate of the hexane of 2%~3% parts by weight, the DA401B tower bottom liquid of 10%~11% parts by weight, the reforming raffinate oil of 7%~8% parts by weight and the C9 aromatic hydrocarbons of 14%~16% parts by weight are added in Mixer pot and are stirred, stirring is at least after ten minutes, at least 4 hours are stood again, it can be used.The present invention is detected, and reconciles out No. 92 gasoline for meeting national standard, has simple process, and condition is easily achieved, and resource consumption is few;Solves naphtha surplus, it is difficult to utilize, it is difficult to which the problem of selling isolates isopentane for blended gasoline, greatly increase its utility value;Product is as clear as crystal, high-quality, and stability is high;The good environmental protection of product can reduce the discharge of pernicious gas in tail gas.
Description
Technical field
It is the invention belongs to chemical field, in particular to a kind of to utilize isopentane reconciliation High-octane mogas and its preparation
Method.
Background technique
Motor petrol is important traffic fuel, and yield accounts for about the 20% of crude runs, mainly there is the chain of C5~C11
Alkane, cycloalkane, alkene, aromatic hydrocarbons and a small amount of sulfur-bearing, nitrogen, oxygen heteroatom compound composition.
Aromatic hydrocarbons can aggravate the carbon distribution of automobile cylinder, increase tail gas discharge capacity, improve CO, HC, NO concentration in tail gas, break annular space
Ozone in gas;Aromatic hydrocarbons incomplete combustion can also generate carcinogen.Alkene is a kind of unstable material, easily in engine oil inlet
Colloid and precipitating are generated in system, nozzle and cylinder, are declined engine efficiency, are influenced its service life, while increasing in tail gas
PM content.
It is influenced by naphtha surplus, naphtha preparation amount of plan is lower, results in naphtha component quilt well below production capacity
It is forced into diesel component or calls in gasoline.If calling in gasoline, because naphtha octane number is low, need to consume the toluene of a large amount of high prices
With BTX aromatics component, reconcile at high cost.In addition, there is sulfur content and the exceeded feelings of olefin(e) centent in gasoline harmonic process sometimes
Condition, it is also necessary to be reconciled with part naphtha, which increases the consumption of high-octane rating blend component, increase and are produced into
This.
Isopentane has RON (93.2) and MON (90.8) relatively high, and anti-knock index is high, can provide enough burnings
Calorific value reduces the discharge of pernicious gas in tail gas, and the advantages of non-aromatics/olefin compound, therefore, isolates in naphtha
Isopentane component is a kind of extraordinary gasoline accord method for the scheme of blended gasoline.
Summary of the invention
It is an object of the invention to produce and reach the one of relevant national standard using isopentane as gasoline blend component
Kind High-octane mogas and preparation method.
To achieve the above object, following technical scheme of the present invention are as follows: a kind of High-octane mogas, including
The component of following weight percentage:
5%~15% isopentane, 40%~45% S_ZORB treated gasoline, 8%~9% high pressure heavy naphtha,
4%~5% methyl tertiary butyl ether(MTBE), 2%~3% light raffinate of hexane, 10%~11% DA401B tower bottom liquid, 7%~8%
Reforming raffinate oil and 14%~16% C9 aromatic hydrocarbons.
The purity of the isopentane is 99%.
Isopentane, S_ZORB are refined vapour under normal temperature and pressure conditions by a kind of preparation method of High-octane mogas
Oil, high pressure heavy naphtha, methyl tertiary butyl ether(MTBE), the light raffinate of hexane, DA401B tower bottom liquid, reforming raffinate oil and C9 aromatic hydrocarbons are added to
It is stirred, then is stood to get purpose product in Mixer pot.
The mixing time is more than or equal to 10min.
The time of repose is more than or equal to 4h.
S_ZORB treated gasoline, methyl tertiary butyl ether(MTBE), the light raffinate of hexane, DA401B tower bottom liquid, is reformed high pressure heavy naphtha
It raffinates oil, C9 aromatic hydrocarbons is Yangtze petroleum chemicals.
The invention has the advantages that (1) simple process, condition are easily achieved, resource consumption is few;(2) naphtha mistake is solved
It is surplus, it is difficult to utilize, it is difficult to which that the problem of selling isolates isopentane for blended gasoline, greatly increase its utility value;
(3) it is detected, reconciles out No. 92 gasoline for meeting national standard;(4) product is as clear as crystal, high-quality, and stability is high;(5) it produces
The good environmental protection of product can reduce the discharge of pernicious gas in tail gas.
Specific embodiment
Detailed description of the preferred embodiments below, it should be noted however that following embodiment is only
It is for illustrating the present invention is that a kind of isopentane reconciles the preparation method of High-octane mogas, protection model of the invention
It encloses and is not limited to these specific embodiments, but determined by claims.
Embodiment 1
Using the preparation method of isopentane reconciliation High-octane mogas, include the following steps: in normal temperature and pressure conditions
Under, by the isopentane of weight percentage 6.55%, 43.67% S_ZORB treated gasoline, 8.73% high pressure heavy naphtha,
4.37% methyl tertiary butyl ether(MTBE), the 2.18% light raffinate of hexane, 10.92% DA401B tower bottom liquid, 7.86% reformation take out
Excess oil and 15.72% C9 aromatic hydrocarbons are added in Mixer pot and are stirred, and stirring at least after ten minutes, then stands at least 4 hours,
Sampling carries out assay from Mixer pot.The non-industrial products of isopentane are the isopentane of 99% purity;The S_ZORB
Treated gasoline, high pressure heavy naphtha, methyl tertiary butyl ether(MTBE), the light raffinate of hexane, DA401B tower bottom liquid, reforming raffinate oil, C9 aromatic hydrocarbons
It is Yangtze petroleum chemicals.
Embodiment 2
Using the preparation method of isopentane reconciliation High-octane mogas, include the following steps: in normal temperature and pressure conditions
Under, by the isopentane of weight percentage 10.46%, 41.84% S_ZORB treated gasoline, 8.37% high pressure scheelite brain
Oil, 4.18% methyl tertiary butyl ether(MTBE), the light raffinate of 2.09% hexane, 10.46% DA401B tower bottom liquid, 7.53% reformation
It raffinates oil and 15.06% C9 aromatic hydrocarbons is added in Mixer pot and is stirred, at least after ten minutes, then to stand at least 4 small for stirring
When, sampling carries out assay from Mixer pot.The non-industrial products of isopentane are the isopentane of 99% purity;The S_
ZORB treated gasoline, high pressure heavy naphtha, methyl tertiary butyl ether(MTBE), the light raffinate of hexane, DA401B tower bottom liquid, reforming raffinate oil, C9
Aromatic hydrocarbons is Yangtze petroleum chemicals.
Embodiment 3
Using the preparation method of isopentane reconciliation High-octane mogas, include the following steps: in normal temperature and pressure conditions
Under, by the isopentane of weight percentage 14.06%, 40.16% S_ZORB treated gasoline, 8.03% high pressure scheelite brain
Oil, 4.02% methyl tertiary butyl ether(MTBE), the light raffinate of 2.01% hexane, 10.04% DA401B tower bottom liquid, 7.23% reformation
It raffinates oil and 14.46% C9 aromatic hydrocarbons is added in Mixer pot and is stirred, at least after ten minutes, then to stand at least 4 small for stirring
When, sampling carries out assay from Mixer pot.The non-industrial products of isopentane are the isopentane of 99% purity;The S_
ZORB treated gasoline, high pressure heavy naphtha, methyl tertiary butyl ether(MTBE), the light raffinate of hexane, DA401B tower bottom liquid, reforming raffinate oil, C9
Aromatic hydrocarbons is Yangtze petroleum chemicals.
Quality index using isopentane reconciliation High-octane mogas of the invention is shown in Table 1.
1 quality index of table
From table 1 it follows that meet national 92# gasoline standard using the motor petrol that isopentane reconciles out, therefore can be with
Example as isopentane reconciliation High-octane mogas.It is empty that utilizing for isopentane has been expanded using isopentane blended gasoline
Between, there is preferable practicability and science.
Although a specific embodiment of the invention is described in detail above in conjunction with the embodiments, need to refer to
Out, the scope of protection of the present invention is not limited by these specific embodiments, but is determined by claims.This
Field technical staff can carry out these embodiments in the range of not departing from technical idea and purport of the invention appropriate
Change, and the embodiment after these changes is obviously also included within protection scope of the present invention.
Claims (5)
1. a kind of High-octane mogas, it is characterised in that the component including following weight percentage:
5%~15% isopentane, 40%~45% S_ZORB treated gasoline, 8%~9% high pressure heavy naphtha, 4%~
5% methyl tertiary butyl ether(MTBE), 2%~3% light raffinate of hexane, 10%~11% DA401B tower bottom liquid, 7%~8% weight
The whole C9 aromatic hydrocarbons raffinated oil with 14%~16%;
The high pressure heavy naphtha, the light raffinate of hexane and DA401B tower bottom liquid are Yangtze petroleum chemicals.
2. motor petrol according to claim 1, it is characterised in that: the purity of the isopentane is 99%.
3. it is a kind of according to claim 1 or the preparation method of motor petrol described in 2 any claims, it is characterised in that: normal
Under the conditions of normal temperature and pressure, by isopentane, S_ZORB treated gasoline, high pressure heavy naphtha, methyl tertiary butyl ether(MTBE), the light raffinate of hexane,
DA401B tower bottom liquid, reforming raffinate oil and C9 aromatic hydrocarbons are added in Mixer pot and are stirred, then stand to get purpose product.
4. preparation method according to claim 3, it is characterised in that: the mixing time is more than or equal to 10min.
5. preparation method according to claim 3, it is characterised in that: the time of repose is more than or equal to 4h.
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Citations (6)
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---|---|---|---|---|
JP2000256682A (en) * | 1999-03-10 | 2000-09-19 | Nippon Mitsubishi Oil Corp | Unleaded gasoline |
CN1572861A (en) * | 2003-06-02 | 2005-02-02 | 金璋晚 | Methanol improved fuel |
CN101177639A (en) * | 2006-11-06 | 2008-05-14 | 上海中茂新能源应用有限公司 | Isopentane vehicle fuel |
CN101200657A (en) * | 2006-12-14 | 2008-06-18 | 金尚汉 | Combustion engine composite fuel and preparation method thereof |
CN104130807A (en) * | 2014-08-14 | 2014-11-05 | 叶景榕 | Ether fuel for vehicle |
CN104673409A (en) * | 2013-12-03 | 2015-06-03 | 华东理工大学 | Lead-free high-quality clean aviation gasoline |
-
2015
- 2015-09-15 CN CN201510585161.6A patent/CN106520219B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000256682A (en) * | 1999-03-10 | 2000-09-19 | Nippon Mitsubishi Oil Corp | Unleaded gasoline |
CN1572861A (en) * | 2003-06-02 | 2005-02-02 | 金璋晚 | Methanol improved fuel |
CN101177639A (en) * | 2006-11-06 | 2008-05-14 | 上海中茂新能源应用有限公司 | Isopentane vehicle fuel |
CN101200657A (en) * | 2006-12-14 | 2008-06-18 | 金尚汉 | Combustion engine composite fuel and preparation method thereof |
CN104673409A (en) * | 2013-12-03 | 2015-06-03 | 华东理工大学 | Lead-free high-quality clean aviation gasoline |
CN104130807A (en) * | 2014-08-14 | 2014-11-05 | 叶景榕 | Ether fuel for vehicle |
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CN106520219A (en) | 2017-03-22 |
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