A process for the production of bio-naphtha from complex mixtures of natural occurring fats & oils
A mixture, naphtha technology, used in the preparation of liquid hydrocarbon mixtures, fatty acid production, biofuels, etc., can solve problems such as corrosion and excessive scaling
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Embodiment 1
[0165] Hydrodeoxygenation of fatty acid feedstock was evaluated under the following conditions.
[0166] In an isothermal reactor, 50 ml of a hydrotreating catalyst consisting of molybdenum and nickel supported on alumina (prepared according to patent US6280610B1) was loaded, the catalyst was dried and used under standard conditions with End-boiling straight-run gas oil (straight-run gas oil is the gas oil fraction obtained directly after distillation without any other treatment) presulfurized. The gas oil is doped with dimethyl disulfide (DMDS). Hydrodeoxygenation of fatty acids is carried out under the following conditions:
[0167] LHSV=1h -1
[0168] Inlet temperature = 320°C
[0169] Outlet pressure = 60 bar
[0170] h 2 / oil ratio = 1050Nl / l
[0171] Feedstock = oleic acid feedstock doped with 2.5 wt% DMDS
[0172] Table 4 shows the typical composition of the oleic acid feedstock.
[0173] The gas and liquid effluents are separated by a separator (gas / liquid) a...
Embodiment 2
[0183] Hydrodeoxygenation of triglyceride feedstock was evaluated under the following conditions:
[0184] In an isothermal reactor, 10 ml of a hydrotreating catalyst (KF848 obtained from Albemarle) consisting of molybdenum and nickel supported on alumina was loaded, the catalyst was dried and washed with straight-run DMDS-doped Gas oil presulfurization. Hydrodeoxygenation of rapeseed oil was carried out under the following conditions:
[0185] LHSV=1h -1
[0186] Inlet temperature = 320°C
[0187] Outlet pressure = 60 bar
[0188] h 2 / oil ratio = 630Nl / l
[0189] Raw material = rapeseed oil doped with 1 wt% DMDS
[0190] Table 6 shows a typical composition of rapeseed oil.
[0191] The gas and liquid effluents are separated by a separator (gas / liquid) at atmospheric pressure. The gas is sent to the μ-GC analyzer and the liquid is sent to the sampler. The mass balance is about 99% and all product weights are calculated for 100 g of treated feedstock.
[0192] Tabl...
Embodiment 3
[0202] N-paraffins and conventional naphtha were steam cracked under different severity conditions. Table 8 presents the results. From the results it is evident that the bio-naphtha thus obtained is a better feedstock for steam cracking than fossil naphtha.
[0203] Significantly higher ethylene and propylene yields can be obtained, however methane production and pyrolysis gasoline production are reduced by at least about 20%. HVC (High Value Chemicals = H 2 +ethylene+propylene+butadiene+benzene) with a final yield higher than 70% by weight. The ethylene / methane weight ratio is always higher than 3.
[0204] Table 8
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[0210] P / E is the ratio of propylene / ethylene
[0211] COT furnace tube outlet temperature
[0212] S / HC is the steam / hydrocarbon ratio
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Abstract
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