CN112646619A - Gasoline product oil - Google Patents
Gasoline product oil Download PDFInfo
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- CN112646619A CN112646619A CN202011445425.5A CN202011445425A CN112646619A CN 112646619 A CN112646619 A CN 112646619A CN 202011445425 A CN202011445425 A CN 202011445425A CN 112646619 A CN112646619 A CN 112646619A
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- Prior art keywords
- gasoline
- oil
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- finished oil
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- 239000003502 gasoline Substances 0.000 title claims abstract description 165
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000011160 research Methods 0.000 claims abstract description 33
- 238000001704 evaporation Methods 0.000 claims abstract description 30
- 230000008020 evaporation Effects 0.000 claims abstract description 30
- 238000009835 boiling Methods 0.000 claims abstract description 13
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 33
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 32
- BZLVMXJERCGZMT-UHFFFAOYSA-N methyl tert-butyl ether Substances COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 claims description 25
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 17
- 230000003197 catalytic effect Effects 0.000 claims description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical group CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 2
- 238000005984 hydrogenation reaction Methods 0.000 claims description 2
- 229910052717 sulfur Inorganic materials 0.000 claims description 2
- 239000011593 sulfur Substances 0.000 claims description 2
- 239000000654 additive Substances 0.000 abstract description 3
- 230000000996 additive effect Effects 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 93
- 239000000446 fuel Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000003350 kerosene Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000282376 Panthera tigris Species 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000010692 aromatic oil Substances 0.000 description 1
- 239000003225 biodiesel Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007655 standard test method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/023—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention discloses gasoline finished oil, wherein the research octane number of the gasoline finished oil is 93-97; the gasoline product oil has an initial boiling point of 30-45 ℃, a 10% evaporation temperature of 50-70 ℃, a 50% evaporation temperature of 98-110 ℃, a 90% evaporation temperature of 155-175 ℃, an end point of not more than 205 ℃ and a residual amount of not more than 1. The gasoline product oil has high heat value, low cost, wide material source, no need of additive, and high safety.
Description
Technical Field
The invention belongs to the field of fuel chemistry, and particularly relates to gasoline product oil.
Background
The finished oil refers to gasoline, kerosene, diesel oil and other alternative fuels which meet the national product quality standard and have the same purpose, such as ethanol gasoline, biodiesel and the like, wherein:
gasoline is the most consumed variety. The boiling point range of the gasoline is 30-205 ℃, and the density of the gasoline is 0.70-0.78 g/cm3The commercial gasoline is marked as 70 octane number, 80 octane number and 80 octane number according to the good and bad anti-knock combustion performance of the gasoline when the gasoline is combusted in a cylinder,90 or higher. The fuel has larger grade and better performance, and is mainly used as the fuel of automobiles, motorcycles, yachts, helicopters and agricultural and forestry aircrafts.
Jet fuel is used primarily for jet aircraft. The boiling point range is 60-280 ℃ or 150-315 ℃ (commonly known as aviation gasoline and aviation kerosene). In order to meet the requirement of high-altitude low-temperature high-speed flight, the oil has large calorific value and does not generate solid crystals at the temperature of minus 50 ℃.
The prior gasoline has no high calorific value, and the jet fuel has high calorific value but high cost, so that a low-cost finished oil with high calorific value is urgently needed.
Disclosure of Invention
The invention aims to provide the gasoline product oil with high heat value and low cost. The gasoline product oil meets the national standard, can be prepared from the conventional raw materials such as raw oil, synthetic oil, fuel oil, oil product additives and the like at will, and only needs the finished product meeting the parameter standard of the application.
The research octane number of the gasoline finished oil is 93-97;
the gasoline product oil has an initial boiling point of 30-45 ℃, a 10% evaporation temperature of 50-70 ℃, a 50% evaporation temperature of 98-110 ℃, a 90% evaporation temperature of 155-175 ℃, an end point of not more than 205 ℃ and a residual amount of not more than 1.
Optionally, the gasoline product oil has an initial boiling point of 30-40 ℃, a 10% evaporation temperature of 50-65 ℃, a 50% evaporation temperature of 98-103 ℃, a 90% evaporation temperature of 160-170 ℃, an end point of 205 ℃ or less, and a residual amount of 1 or less.
Optionally, the initial boiling point of the gasoline product oil is 30-40 ℃.
Optionally, the initial boiling point of the gasoline product oil is 35-40 ℃.
Optionally, the evaporation temperature of 10% of the gasoline finished oil is 55-70 ℃.
Optionally, the evaporation temperature of 10% of the gasoline product oil is 50-70 ℃.
Optionally, the 50% evaporation temperature of the gasoline product oil is 98-108 ℃.
Optionally, the 50% evaporation temperature of the gasoline product oil is 100-110 ℃.
Optionally, the 90% evaporation temperature of the gasoline product oil is 155-175 ℃.
Optionally, the 90% evaporation temperature of the gasoline product oil is 155-175 ℃.
Optionally, the density of the gasoline finished oil is 744-758 kg/m3。
Optionally, the density of the gasoline finished oil is 740-756 kg/m3。
Optionally, the density of the gasoline finished oil is 745-756 kg/m3。
Optionally, the density of the gasoline finished oil is 745-755 kg/m3。
Optionally, the density of the gasoline product oil is 748-753 kg/m3。
Optionally, the density of the gasoline finished oil is 744-755 kg/m3。
Optionally, the density of the gasoline finished oil is 746-758 kg/m3。
Optionally, the sulfur content of the gasoline product oil is less than or equal to 8 mg/kg.
Optionally, the volume percentage of aromatic hydrocarbon in the gasoline product oil is 25-35%.
Optionally, the volume percentage of aromatic hydrocarbon of the gasoline product oil is 30-35%.
Optionally, the volume percentage of aromatic hydrocarbon in the gasoline product oil is 25-33%.
Optionally, the volume percentage of aromatic hydrocarbon of the gasoline product oil is 28-35%.
Optionally, the research octane number of the gasoline finished oil is 93-94.
Optionally, the research octane number of the gasoline finished oil is 93.1-94.5.
Optionally, the research octane number of the gasoline finished oil is 95.5-97.
Optionally, the research octane number of the gasoline finished oil is 96-97.
Optionally, the research octane number of the gasoline-type finished oil is independently selected from any of 93.1, 93.5, 94, 94.5, 95, 95.5, 96, 96.5, 97 or a range between any two.
Optionally, the research octane number of the gasoline finished oil is 93.1-94.9;
the gasoline product oil has an initial boiling point of 30-45 ℃, a 10% evaporation temperature of 50-65 ℃, a 50% evaporation temperature of 98-108 ℃, a 90% evaporation temperature of 155-175 ℃, an end point of not more than 205 ℃ and a residual amount of not more than 1.
Optionally, the density of the gasoline finished oil is 744-755 kg/m3。
Optionally, the volume percentage of aromatic hydrocarbon in the gasoline product oil is 25-33%.
The research octane number of the gasoline finished oil is 95.5-97;
the gasoline product oil has an initial boiling point of 30-40 ℃, a 10% evaporation temperature of 50-70 ℃, a 50% evaporation temperature of 100-110 ℃, a 90% evaporation temperature of 160-175 ℃, an end point of not more than 205 ℃ and a residual amount of not more than 1.
Optionally, the density of the gasoline finished oil is 746-758 kg/m3。
Optionally, the volume percentage of aromatic hydrocarbon of the gasoline product oil is 28-35%.
Optionally, the gasoline-type finished oil comprises at least one of the following components:
hydrogenated catalytic gasoline, dimethylbenzene, mixed benzene, methyl tert-butyl ether, alkylate oil, aromatic hydrocarbon, finished oil No. 92, finished oil No. 95 and naphtha.
Optionally, the research octane number of the hydrocatalytic gasoline is 70-90, and the density is 727-767 kg/m3；
The research octane number of the dimethylbenzene is 115-120, and the density of the dimethylbenzene is 860-868 kg/m3；
The mixed benzene has a research octane number of 105-115 and a density of 851-868 kg/m3；
The research octane number of the methyl tert-butyl ether is 115, and the density of the methyl tert-butyl ether is 740-743 kg/m3；
The research octane number of the alkylate oil is 95, and the density of the alkylate oil is 690-693 kg/m3；
The research octane number of the aromatic hydrocarbon is 92-115, and the density is 754-900 kg/m3；
The research octane number of the finished product oil No. 92 is 92.5-93.2, and the density is 733-738 kg/m3；
The finished product oil 95# has a research octane number of 95-96 and a density of 733-738 kg/m3；
The naphtha has a research octane number of 65-70 and a density of 665-755 kg/m3。
Optionally, the research octane number of the aromatic hydrocarbon is 92-115, and the density is 880-900 kg/m3。
Optionally, the research octane number of the finished oil No. 92 is 92.5-93, and the density is 733-738 kg/m3。
Optionally, the gasoline finished oil comprises the following components in parts by mass:
25-58 parts of hydrogenation catalytic gasoline, 6-26 parts of mixed benzene and 5-11 parts of methyl tert-butyl ether.
Optionally, the gasoline finished oil comprises the following components in parts by mass:
20-40 parts of alkylate oil, 6-20 parts of mixed benzene and 7-16 parts of heavy aromatic hydrocarbon.
Optionally, the research octane number of the heavy aromatic hydrocarbon is 115-120, and the density is 800-900 kg/m3。
Optionally, the gasoline finished oil comprises the following components in parts by mass:
73-87 parts of finished oil and 5-10 parts of heavy aromatic hydrocarbon.
Optionally, the gasoline finished oil comprises the following components in parts by mass:
92# 61-90 parts of finished oil, 0-24 parts of naphtha and 6-15 parts of dimethylbenzene.
In an optional embodiment, the naphtha is 4-11 parts.
Optionally, the gasoline finished oil comprises the following components in parts by mass:
150# carbon ten and 1-10 parts of heavy aromatic oil.
In one embodiment, the naphtha is 4-24 parts, the finished oil is 89# 20-30 parts, the 150# decaaromatic hydrocarbon oil is 1-10 parts, and the aromatic hydrocarbon is 22-38 parts.
Optionally, the gasoline-type finished oil comprises the following components:
hydrogenated catalytic gasoline, alkylate oil, mixed benzene and methyl tert-butyl ether.
Optionally, the gasoline-type finished oil comprises the following components:
alkylate, mixed benzene, methyl tert-butyl ether, aromatic hydrocarbon, and naphtha.
Optionally, the gasoline-type finished oil comprises the following components:
finished oil 92#, aromatic hydrocarbons, naphtha.
Optionally, the gasoline-type finished oil comprises the following components:
alkylate, mixed benzene, methyl tert-butyl ether, aromatic hydrocarbon, and naphtha.
Optionally, the gasoline-type finished oil comprises the following components:
hydrogenated catalytic gasoline, alkylate oil, mixed benzene, methyl tert-butyl ether, aromatic hydrocarbon and naphtha.
Optionally, the gasoline-type finished oil comprises the following components:
hydrogenated catalytic gasoline, alkylate oil, mixed benzene, aromatic hydrocarbon and naphtha.
Optionally, the gasoline-type finished oil comprises the following components:
mixed benzene, finished oil 92#, aromatic hydrocarbon and naphtha.
Optionally, the gasoline-type finished oil comprises the following components:
hydrogenated catalytic gasoline, alkylate oil, mixed benzene, methyl tert-butyl ether and naphtha.
Optionally, the gasoline-type finished oil comprises the following components:
mixed benzene, finished oil 95# and aromatic hydrocarbon.
Optionally, the gasoline-type finished oil comprises the following components:
alkylate oil, mixed benzene, finished oil No. 92 and aromatic hydrocarbon.
Optionally, the gasoline-type finished oil comprises the following components:
alkylate, xylene, methyl tert-butyl ether, aromatics, naphtha.
In this application, unless otherwise indicated, the data ranges given are selected from any value within the range, and include the endpoints of the range.
In this application, MTBE refers to methyl tert-butyl ether.
Benefits that can be produced by the present application include, but are not limited to:
the gasoline product oil has high heat value, low cost, wide material source, no need of additive, and high safety.
Detailed Description
The present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples.
The raw materials used in the embodiments of the invention are all commercial products, and the gasoline product oil in the embodiments is prepared by mixing the raw materials.
In the present application, the aromatic hydrocarbon includes coal-to-aromatics, aromatic hydrocarbons, coal-based heavy aromatic hydrocarbons, and heavy aromatic hydrocarbons, which are commonly used in the art. Heavy aromatics can be further classified into nona-and deca-carbon aromatics.
In the following examples, hydrocatalytic gasoline is abbreviated as hydrocatalytic gasoline and alkylate oil is abbreviated as alkylate.
In the examples, the proportions refer to the mass parts of the components.
In the examples, the density units are g/cm3。
In the examples, the density sum is the product of the component mass ratio and the density itself.
In the examples, the octane sum is the product of the mass ratio of the components and the octane number itself.
In the examples, the total density value of the blend oil product is the sum of the density sum values of the components, and the total octane value of the blend oil product is the sum of the octane sum values of the components.
Example 1
Example 2
Example 3
Example 4
Example 5
Example 6
Example 7
Example 8
Example 9
Example 10
Example 11
Example 12
Example 13
Example 14
Example 15
Example 16
Example 17
Example 18
Example 19
Example 20
The names of the manufacturers in the above embodiments are the names of the manufacturers purchasing the corresponding raw materials, and the density units are kg/m3The proportions are mass percentages. Wherein the gasoline of No. 92 is obtained in examples 1-12, 17 and 18, and the gasoline of No. 95 is obtained in examples 13-16, 19 and 20.
The gasoline product oil obtained in each example is subjected to performance test, and the test method refers to the national standard for motor gasoline (GB 17930-2016). The test site is Ningxia Yinchuan, the altitude is 1010 meters, and the atmospheric pressure is 896 hpa.
Table 1 shows the index data for blend gasoline # 92.
Table 2 shows the index data for 95# blend gasoline.
It should be noted that, because of different regions, corresponding altitude, atmospheric pressure, etc., there are certain differences, but according to the national standard test method, the parameters standards given by the national standard and the present application are all satisfied after corresponding conversion.
(distillation range experiment method according to petrochemical industry standard, corresponding adjustment is needed according to local atmospheric pressure, the numerical values in the case already contain atmospheric pressure influence factors.)
The test results show that the gasoline product oil provided by each embodiment meets the following requirements:
standard requirements met by Table 392 # blended gasoline
TABLE 495 # blend gasoline meets the standard requirements
The gasoline product oil provided by the embodiment of the application is obviously reduced in fuel consumption per hundred kilometers and the refueling cost compared with the conventional gasoline with the same model under the same driving condition after being tried out by tens of users, wherein:
1. compared with 54.59 liters of 92# gasoline purchased from the market, the 53.56 liters of 92# gasoline prepared by the method in the embodiment 1 of the application has the vehicle type of Chevrolet, the running mileage of the gasoline prepared by the method is 646.6 kilometers, and the running kilometers of the gasoline purchased from the market are 574 kilometers;
2. compared with 64.99 liters of 95# gasoline purchased on the market, the model of the 64.58 liters of 95# gasoline prepared by the embodiment 13 of the application is Benz E300L, the running mileage of the gasoline prepared by the application is 580 kilometers, and the running kilometers of the gasoline purchased on the market are 508 kilometers;
3. compared with 75.2 liters of 95# gasoline purchased from the market, the 75 liters of 95# gasoline prepared by the embodiment 13 of the application has the vehicle type of strap-down XFL, the running mileage of the gasoline prepared by the application is 661 kilometers, and the running kilometers of the gasoline purchased from the market are 623 kilometers;
4. compared with 38.19 liters of 92# gasoline purchased from the market, the 38.14 liters of 92# gasoline prepared by the embodiment 4 of the application has a model of Changan Mazda, the running mileage of the gasoline prepared by the application is 518 kilometers, and the running kilometers of the gasoline purchased from the market are 468 kilometers;
5. compared with the 54.98L 92# gasoline purchased from the market, the 54.98L 92# gasoline prepared by the embodiment 4 of the application has the model of Jili Dihao, the gasoline prepared by the application has the travel mileage of 709 kilometers, and the travel kilometers of the gasoline purchased from the market are 648 kilometers;
6. compared with 61.92 liters of 92# gasoline purchased from the market, the 61.92 liters of 92# gasoline prepared by the embodiment 5 of the application has the vehicle type of Toyota Hanlanda, the running mileage of the gasoline prepared by the application is 606 kilometers, and the running kilometers of the gasoline purchased from the market are 509 kilometers;
7. compared with the gasoline No. 92 of 46.98 liters purchased from the market, the gasoline No. 92 of 46.98 liters prepared by the method of the embodiment 5 of the application has the vehicle type of Skodak, the running mileage of the gasoline prepared by the method is 854 kilometers, and the running kilometers of the gasoline purchased from the market is 788 kilometers;
8. compared with 51.52 liters of 92# gasoline purchased on the market, the 52.48 liters of 92# gasoline prepared by the embodiment 6 of the application has the vehicle type of Volkswagen Santana, the running mileage of the gasoline prepared by the application is 778 kilometers, and the running kilometers of the gasoline purchased on the market is 684 kilometers;
9. compared with 51.54L 92 gasoline purchased from the market, the 52.35L 92 gasoline prepared by the embodiment 6 of the application has a Ford tiger model, the gasoline prepared by the application has a mileage of 497 kilometers, and the gasoline purchased from the market has a kilometer number of 455 kilometers;
10. compared with 40 liters of 92# gasoline purchased on the market, the 40.03 liters of 92# gasoline prepared by the embodiment 7 of the application has the Scokada crystal sharp model, the running mileage of the gasoline prepared by the application is 511 kilometers, and the running kilometers of the gasoline purchased on the market are 442 kilometers;
11. compared with 42.43 liters of 92# gasoline purchased from the market, the 42.69 liters of 92# gasoline prepared by the embodiment 7 of the application has the vehicle type of Jili Jiaji, the gasoline running mileage regulated by the application is 496 kilometers, and the running kilometers of gasoline purchased from the market are 454 kilometers;
12. compared with 43 liters of 92# gasoline purchased on the market, the 42.61 liters of 92# gasoline prepared by the embodiment 8 of the application is Toyota Kara, the running mileage of the gasoline prepared by the application is 542 kilometers, and the running mileage of the gasoline purchased on the market is 493 kilometers.
13. Compared with 35.22 liters of 92 gasoline purchased from the market, the 35.22 liters of 92 gasoline prepared by the embodiment 8 of the application has the vehicle type of Pengling sunlight, the gasoline running mileage of the gasoline prepared by the application is 557 kilometers, and the running kilometers of the gasoline purchased from the market are 487 kilometers.
Although the present application has been described with reference to a few embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the application as defined by the appended claims.
Claims (10)
1. The gasoline product oil is characterized in that the research octane number of the gasoline product oil is 93-97;
the gasoline product oil has an initial boiling point of 30-45 ℃, a 10% evaporation temperature of 50-70 ℃, a 50% evaporation temperature of 98-110 ℃, a 90% evaporation temperature of 155-175 ℃, an end point of not more than 205 ℃ and a residual amount of not more than 1.
2. The gasoline-based finished oil of claim 1, wherein the density of the gasoline-based finished oil is 744-758 kg/m3；
Preferably, the aromatic hydrocarbon volume percentage content of the gasoline finished oil is 25-35%;
preferably, the sulfur content of the gasoline product oil is less than or equal to 8 mg/kg.
3. The gasoline-based finished oil according to claim 1, wherein the research octane number of the gasoline-based finished oil is 93.1-94.9;
the initial boiling point of the gasoline product oil is 30-45 ℃, the 10% evaporation temperature is 50-65 ℃, the 50% evaporation temperature is 98-108 ℃, the 90% evaporation temperature is 155-175 ℃, the final boiling point is less than or equal to 205 ℃, and the residual quantity is less than or equal to 1;
preferably, the density of the gasoline finished oil is 744-755 kg/m3；
Preferably, the aromatic hydrocarbon volume percentage content of the gasoline finished oil is 25-33%.
4. The gasoline-based finished oil according to claim 1, wherein the research octane number of the gasoline-based finished oil is 95.5-97;
the gasoline product oil has a primary boiling point of 30-40 ℃, a 10% evaporation temperature of 50-70 ℃, a 50% evaporation temperature of 100-110 ℃, a 90% evaporation temperature of 160-175 ℃, an end point of not more than 205 ℃ and a residual amount of not more than 1;
preferably, the density of the gasoline finished oil is 746-758 kg/m3；
Preferably, the aromatic hydrocarbon volume percentage content of the gasoline finished oil is 28-35%.
5. The gasoline-based product oil of claim 1, wherein the gasoline-based product oil comprises at least one of the following components:
hydrogenated catalytic gasoline, dimethylbenzene, mixed benzene, methyl tert-butyl ether, alkylate oil, aromatic hydrocarbon, finished oil No. 92, finished oil No. 95 and naphtha.
6. The gasoline product oil of claim 5, wherein the hydrogenated catalytic gasoline has a research octane number of 70-90 and a density of 727-767 kg/m3；
The research octane number of the dimethylbenzene is 115-120, and the density of the dimethylbenzene is 860-868 kg/m3；
The mixed benzene has a research octane number of 105-115 and a density of 851-868 kg/m3；
The research octane number of the methyl tert-butyl ether is 115, and the density of the methyl tert-butyl ether is 740-743 kg/m3；
The research octane number of the alkylate oil is 95, and the density of the alkylate oil is 690-693 kg/m3；
The research octane number of the aromatic hydrocarbon is 92-115, and the density is 754-900 kg/m3；
The research octane number of the finished product oil No. 92 is 92.5-93.2, and the density is 733-738 kg/m3；
The finished product oil 95# has a research octane number of 95-96 and a density of 733-738 kg/m3；
The naphtha has a research octane number of 65-70 and a density of 665-755 kg/m3。
7. The gasoline-based finished oil according to claim 1, wherein the gasoline-based finished oil comprises the following components in parts by mass:
25-58 parts of hydrogenation catalytic gasoline, 6-26 parts of mixed benzene and 5-11 parts of methyl tert-butyl ether.
8. The gasoline-based finished oil according to claim 1, wherein the gasoline-based finished oil comprises the following components in parts by mass:
20-40 parts of alkylate oil, 6-20 parts of mixed benzene and 7-16 parts of heavy aromatic hydrocarbon.
9. The gasoline-based finished oil according to claim 1, wherein the gasoline-based finished oil comprises the following components in parts by mass:
73-87 parts of finished oil and 5-10 parts of heavy aromatic hydrocarbon.
10. The gasoline-based finished oil according to claim 1, wherein the gasoline-based finished oil comprises the following components in parts by mass:
92# 61-90 parts of finished oil, 0-24 parts of naphtha and 6-15 parts of dimethylbenzene.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010117082 | 2020-02-25 | ||
| CN2020101170823 | 2020-02-25 |
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| CN112646619A true CN112646619A (en) | 2021-04-13 |
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| CN202011445425.5A Pending CN112646619A (en) | 2020-02-25 | 2020-12-08 | Gasoline product oil |
| CN202011552342.6A Pending CN112646620A (en) | 2020-02-25 | 2020-12-24 | Blended gasoline product oil |
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Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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