Method and system for producing clean gasoline
A gasoline and clean technology, applied in the treatment of hydrocarbon oil, petroleum industry, hydrocarbon oil treatment products, etc., can solve the problems of increasing investment, increasing hydrogen consumption, reducing the octane number of catalytic gasoline of etherification products, etc.
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Embodiment 1
[0074] A system for the production of clean gasoline: with such figure 2 structure shown.
[0075] The method for producing clean gasoline: the etherification catalyst used in the etherification process is a macroporous sulfonic acid cation exchange resin commercially purchased from Dandong Mingzhu Special Resin Co., Ltd., and the trade name is D005-ⅡS; the specific process flow is as follows:
[0076] The above-mentioned full fraction gasoline raw material 1 is mixed with hydrogen 2 and then transported to the refining reactor 3 (fluidized bed reactor), at a temperature of 429 ° C, a pressure of 2.6 MPa, and a volume space velocity of 6.5 h -1 , the volume ratio of hydrogen to hydrocarbons is under the hydrogen refining reaction conditions of 0.28, and the contact reaction with the refining agent obtains the refined reaction product 4; the refined reaction product 4 removes hydrogen and part of the following components of C4 through the light removal tower (tank) 5 6 Finall...
Embodiment 2
[0078] Systems for Producing Clean Gasoline: See figure 2 In the structure shown, the difference is that part of the isomerization product 36 is sent to the secondary etherification reactor 20 , and the rest is returned to the primary etherification reactor 13 .
[0079] The method for producing clean gasoline: with reference to Example 1, the difference is that the etherification catalyst used is a catalyst containing Y-type molecular sieves, and the catalyst preparation method refers to the document CN 105080589A; the etherification reaction temperature is 60-80 ° C; in addition, in two In the primary etherification reactor, the molar ratio of alcohol to active olefin in the mixture of the overhead azeotrope and the isomerization product is adjusted to 1.5:1, and the excess isomerization product is returned to the primary ether chemical reactor. The blended clean gasoline is denoted as S2, and the properties of the product are shown in Table 3.
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