CN1257960C

CN1257960C - Process for preparing liquefied propane gas and gasoline with high octane value from plant fibres

Info

Publication number: CN1257960C
Application number: CN 01138935
Authority: CN
Inventors: 丛大拥
Original assignee: Individual
Current assignee: Individual
Priority date: 2001-12-27
Filing date: 2001-12-27
Publication date: 2006-05-31
Anticipated expiration: 2021-12-27
Also published as: CN1360007A

Abstract

The present invention relates to a method for preparing a propane liquefied gas and high-octane petrol by utilizing plant fibers, which comprises the following steps that plant fibers (such as corn straw, rice straw, reeds, etc.) generate a mix gas of carbon monoxide and propane by vacuum dry distillation cracking reaction; the mixed gas of the carbon monoxide and the propane is separated by adopting a PSA pressure swing adsorption method to respectively generate and purify hydrogen gases, to recovery carbon dioxide and to prepare propane liquefied gases; methanol is synthesized by the CO, CO2, H2 prepared by the steps with an ICI low pressure method; finally, the methanol is made into gasoline by adopting an MTG method. The ideal mixed gas is obtained by adopting the vacuum cracking technology, so the impurities are fewer; biotic substance cellulose is taken as a raw material, so the cost is low, and the resources are wide; the present invention is a regenerable new resource and has sustainable development and environmental protection.

Description

Utilize vegetable fibre to produce the method for stop bracket gasoline

Technical field:

The present invention discloses a kind of method of utilizing vegetable fibre to produce stop bracket gasoline, relates to the technical field that vegetable fibre is converted into hydrocarbon fuel.

Background technology:

Utilize dry distillation that vegetable fibre (as maize straw, straw, reed etc.) is produced civilian combustible gas by retort in China and be applied, owing to issue biochemical reaction at atmospheric pressure state, the combustible gas component more complicated of generation is CO, CO ₂, multiple gases such as nitrogen, hydrogen, methane, do not have the propane composition, though the calorific value of methane is 39.819MJ/m ³, but with propane calorific value (101.242MJ/m ³) compare and fall far short, in adding gas mixture, also contain the inert nitrogen about 10%, then seriously influenced the burning quality of combustible gas;

Being to adopt fermentation method earlier grain to be made methyl alcohol in the world, producing hydrocarbon fuel again, is that the employing corn is that application MTG legal system was got gasoline after raw material generated methyl alcohol as the U.S..The Brazilian SaSOI company in South Africa is that to use sugarcane be that raw material generates and uses the MTG legal system behind the methyl alcohol and get gasoline, above-mentioned complex process, and cost is higher, can not get actual applying.

Summary of the invention:

The present invention discloses a kind of method of utilizing vegetable fibre system to change liquefied propane gas, carries out the carbonization decomposition reaction and produce liquefied propane gas under vacuum state; Utilize the method for the synthetic stop bracket gasoline of above-mentioned LNG gasifaction again;

Technical solution of the present invention may further comprise the steps:

1, dry vacuum distillation scission reaction:

The vegetable fibre straw is pulverized after drying remove inside and outside moisture content, temperature is 105 ℃-115 ℃, the retort equipment of putting into, and adding supplies pulverized anthracite, add-on is the 22-23% that the vegetable fibre straw is pulverized dry back weight, and the carbonization decomposition reaction is carried out gradient from 300 ℃-500 ℃ and heated under the vacuum state, reaction times is 2.5 to 3 minutes, gets carbon monoxide and propane gas mixture.

2, adopt the PSA pressure swing adsorption process that carbon monoxide is separated with the propane mixed gas;

Processing condition are: mixture temperature is 50 ℃-80 ℃, pressure is 0.1-0.15Mpa, and carbon monoxide reclaim under reduced pressure pressure is 6-13Kpa, and sorption cycle cycle 12-20min purge gas is than (flushing dose/air-fuel mixture amount) 0.3-0.7, carbon monoxide is pure to be 98～99%, and yield is greater than 80%.

3, produce liquefied propane gas:

Adopt absorption method, as sorbent material, the temperature of desorption is 235 ℃～265 ℃ with gac, and desorption gas is recyclable hydro carbons through condensation separation, obtains purified propane gas.

Utilize above-mentioned production method to proceed technical process and produce stop bracket gasoline: step is as follows:

1, the generation of hydrogen:

60% of isolated carbon monoxide is added the excessive water steam carry out that conversion generates hydrogen and carbon dioxide is stand-by, and be that the carbon monoxide that has neither part nor lot in conversion is used for hydrogenation and generates methyl alcohol and prepare.

The catalyzer that conversion is used has two kinds of middle temperature transformation and low temperature shift catalysts.Medium temperature shift catalyst commonly used has the siderochrome catalyzer, and (major ingredient is Fe ₂O ₃, Cr ₂O ₃Active temperature is 450 ℃-500 ℃) or ferro-magnesium catalyst (major ingredient is Fe ₂O ₃, the MgO active temperature is 350 ℃-500 ℃).Low temperature shift catalyst has copper zinc chrome catalyzer, and (major ingredient is CuO, ZnO, Cr ₂O ₃) or CuZnAl catalyst (major ingredient is CuO, ZnO, Al ₂O ₃) in 170 ℃ of-280 ℃ of scopes of its active temperature.

2, the purification of hydrogen; The hydrogen of gained is purified by the PSA pressure swing adsorption process.

3, carbon dioxide recovery; Adopt pressure swing adsorption process with carbon dioxide recovery.

4, methyl alcohol is synthetic:

CO, CO that above-mentioned steps is made ₂, H ₂Adopt the ICI low-pressure process to carry out the synthetic of methyl alcohol, catalyzer is an oxycompound, synthesizing methanol under the condition of 240 ℃～270 ℃ temperature, 5MPa pressure;

5, the generation of stop bracket gasoline:

Adopt the MTG method that methyl alcohol is made gasoline, the MTG process has two kinds of beds, be fixed bed and fluidized-bed, in fixed-bed process, reaction divides two sections to carry out: first section is reflected at pressure is that 1.3-2.3Mpa and temperature are to be the dme equilibrium products with methanol dehydration under 300-400 ℃, enter subordinate phase then, the cracking reactor of ZSM-5 zeolite [molecular sieve is housed.Temperature of reaction 340-450 ℃, with the circulation of light gas hydrocarbon, remove partial reaction heat, with the control thermal insulation warming.

Can use fuel-grade methyl alcohol to be raw material.Weight hourly space velocity is 0.15-1.5 (to a methyl alcohol) to catalyst for cracking.

Can get gasoline 86%, motor-method octane number MON is 93.

Positively effect of the present invention is: the employing biomass cellulose is a raw material, and cost is cheap, and resource is extensive, and be can Sustainable development the reproducible new resources of environment-friendly type.Carbonization decomposition can obtain to contain the mixed gas of propane under vacuum state, and impurity is less, and gas heating value significantly improves, and not only can directly burn, and can also reach the engine gas standard.

Embodiment:

Embodiment 1

Get corn stalk, being ground into particulate state and auxiliary material hard coal mixes all, drying is removed internal moisture under 105 ℃～115 ℃ temperature, straw 100kg, hard coal 22kg after the drying are put into the dry vacuum distillation still, temperature is 300 ℃～500 ℃ gradient increased temperatures, carry out scission reaction, the reaction times is 2.5 minutes, and per 4 kilograms of raw materials can obtain 1m ³The mixed combustible gas body, wherein 30% is propane gas, 70% is CO gas.

Adopt PSA four bed pressure swing adsorption process with the disposable separation of CO.Process conditions: the unstripped gas temperature is 50～80, pressure 0.1～0.5Mpa, and CO reclaim under reduced pressure pressure is 6～13Kpa, adsorption cycle 12～20min, purge gas is than (flushing dose/material quantity) 0.3～0.7.The CO product purity is 98～99%, and the rate of recovery is greater than 80%.

60% add excessive water vapour under temperature is 400～480 ℃, the effect of catalyzer with what isolate CO, react and generate hydrogen and carbonic acid gas.

Adopt siderochrome catalyzer in the medium temperature shift catalyst, main component weight % is Fe ₂O ₃: 89 ± 2, Cr ₂O ₃: 9 ± 2, active temperature is 450 ℃～500 ℃, air speed: 2000 hours ^-1Input amount; Middle temperature transformation tower diameter is 1.4 meters, and height is 6.09 meters, daily output 410kgH ₂, need catalyzer 5.39m ³

Gained hydrogen by six transformation absorption of PSA purifying hydrogen of hydrogen device, is purified to hydrogen, and purity is 99.59%, and yield can reach more than 86%.

The physics method is adopted in the recovery of carbonic acid gas, and both transformation absorption method of purification reclaimed C ₂Purity greater than 99.5%.

Producing liquefied propane gas employing absorption method is sorbent material with the gac, 1.5 meters of carbon-coating height, and logistics speed 6cm/S with three adsorber alternate operations, can obtain to manage hot purified C3 gas.In critical-point pressure is 4.15Mpa, and liquefaction when temperature is 96.67 ℃ produces liquefied propane gas.

Synthesizing of methyl alcohol: will remain 40% carbon monoxide in the material mixed gas and generate carbonic acid gas and the hydrogen that produces in the hydrogen engineering, with ICI low-pressure process generation methyl alcohol, formation condition be: pressure 5Mpa, 200 ℃～270 ℃ of temperature, use CuZnAl catalyst (main component CuO, ZnO, Al ₂O ₃), form copper 70%, aluminium 10%, zinc 20%, air speed is 10000 ^-1, input amount: with LC300 type synthesizer, 1.5 tons of/hour methyl alcohol of output need 1m ³Catalyzer.

Adopt fixed-bed process in the MTG method, first section is reflected at pressure is that 1.3～2.3Mpa and temperature are to be the dme equilibrium products with methanol dehydration under 300 ℃～450 ℃, enter subordinate phase then, with the ZSM-5 zeolite molecular sieve methyl alcohol is carried out scission reaction and make gasoline, 340 ℃～450 ℃ of temperature of reaction, can obtain gasoline, motor-method octane number MON is 93, and yield is 86%.

Claims

1, a kind of method of utilizing vegetable fibre to produce stop bracket gasoline, comprise vegetable fibre is generated propane flammable gas and carbon mono oxide mixture in the dry vacuum distillation scission reaction, and adopt the PSA pressure swing adsorption process that CO (carbon monoxide converter) gas is separated, it is characterized in that also comprising the steps to produce gasoline;

1) generation of hydrogen:

Isolate the carbon monoxide that accounts for carbon monoxide and propane gas mixture total amount 70%, wherein 60% of CO adds excessive water vapour and reacts and generate hydrogen and carbonic acid gas;

2) collect hydrogen, adopt the PSA pressure swing adsorption process that hydrogen is purified;

3) adopt pressure swing adsorption process with carbon dioxide recovery;

4) methyl alcohol is synthetic:

CO, CO that above-mentioned steps is made ₂, H ₂Adopt the ICI low-pressure process to carry out the synthetic of methyl alcohol, catalyzer is an oxycompound, synthesizing methanol under the condition of 240 ℃～270 ℃ of temperature, 5MPa pressure;

5), the generation of stop bracket gasoline:

Adopt the MTG method that methyl alcohol is made gasoline.