Method for efficient resource utilization of tank bottom oil sludge
A technology of recycling and oil sludge, applied in chemical instruments and methods, petroleum industry, sludge treatment, etc., can solve the problems of incomplete treatment, waste of resources, high cost, etc., to promote oil production rate, reduce treatment cost, increase Yield effect
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Embodiment 1
[0032] The fresh tank bottom sludge is subjected to dehydration pretreatment. The process is as follows: the fresh tank bottom sludge is exposed to sunlight to evaporate part of the water. The exposure time is 8 days. During the exposure process, part of the fresh tank bottom sludge Crude oil is precipitated, and the precipitated crude oil is recovered and collected, and the remaining raw material is the raw material for liquefaction of tank bottom sludge. The raw material for liquefaction of oil sludge at the bottom of the tank obtained in Blank Example 1 was analyzed by an elemental analyzer, and the analysis results are shown in Table a.
[0033] table a
[0034]
[0035]The oil content, water content, and solid content of the tank bottom sludge liquefaction raw material obtained in Blank Example 1 were tested, and the results are shown in Table b.
[0036] table b
[0037]
[0038] Example 1:
[0039] use as figure 1 The shown liquefaction device reacts. In this ...
Embodiment 2
[0057] use as figure 1 The shown liquefaction device reacts. In this embodiment, under the condition of adding catalyst A, the recovery effect of tank bottom oil sludge liquefaction resources under the best conditions is explored. The operation process is as follows (the process flow chart is as follows figure 2 shown):
[0058] S1: Pyrolyze fresh rice husks, put dry rice husks into a muffle furnace at 500°C for 1.0 hour under an argon atmosphere, grind them into powder after cooling, and pass through a 100-mesh sieve to make biochar powder. The obtained biochar powder was mixed with ethanol according to the mass ratio of 1.1:18.9 to obtain catalyst A.
[0059] S2: Mix the tank bottom sludge liquefaction raw material obtained in Blank Example 1, Catalyst A and water according to the mass percentage, and then place it in the tank bottom sludge reaction kettle, feed argon gas until the initial pressure is 3.0 MPa, and then close the tank bottom sludge reactor , carry out the...
Embodiment 3
[0074] use as figure 1 The shown liquefaction device reacts. In this example, under the condition of only ethanol or only adding biochar, the effect of recovery of tank bottom sludge liquefaction resources is explored. The operation process is as follows:
[0075] S1: Mix the tank bottom sludge liquefaction raw material obtained in Blank Example 1 with water according to the mass percentage, then place it in the tank bottom sludge reactor, add ethanol or biochar, feed argon until the initial pressure is 3.0MPa, and then react the tank bottom sludge The kettle is closed, the heating temperature for the liquefaction reaction is set to 300°C, and the reaction time is 30 minutes;
[0076] Wherein: when only ethanol is added, the mass percentage of the tank bottom sludge liquefaction raw material is 9.6%, the mass percentage of water is 47.9%, the mass percentage of ethanol is 42.5%, and the sum of the mass percentages of each component is 100%; when only biochar is added (biochar...
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