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129results about How to "Reduce Methanol Content" patented technology

Process for refining C-4 hydrocarbon fluid

The invention discloses a process for refining C-4 hydrocarbon fluid. Preparation equipment includes a methanol removing tower, a first hydrogenation reactor, a second hydrogenation reactor, a depropanizing column, a dethanizing column and an adsorption tower, wherein the top of the methanol removing tower is connected with the bottom of the first hydrogenation reactor through a high-efficiency coalescer; the top of the first hydrogenation reactor is connected with the bottom of the second hydrogenation reactor through a pipeline; the top of the second hydrogenation reactor is connected with the depropanizing column through another pipeline; the top of the depropanizing column is connected with the dethanizing column through another pipeline; and the bottom of the dethanizing column is connected with the adsorption tower through another pipeline. The process mainly aims to a purification process of an alkylation raw material, and comprises the following steps: by taking mixed C-4 hydrocarbon as a raw material, extracting with water to remove methanol so as to reduce the content of methanol in C-4 hydrocarbon to be lower than 50ppm, selectively adding hydrogen and isomerizing so as to reduce the content of butadiene in C-4 hydrocarbon to be lower than 50ppm, converting more than 70% of 1-butene into 2-butene, and finally rectifying to remove dimethyl ether and C-3, thereby obtaining refined C-4 as the alkylation raw material, and a byproduct refined C-3 as a propane dehydrogenation propylene raw material.
Owner:CHINA CHENGDA ENG

Method for brewing white spirit by adopting red dates as major ingredient

The invention discloses a method for brewing white spirit by adopting red dates as a major ingredient. In the invention, the white sprit is prepared by taking fresh or dry red dates as the major ingredient and bran as an auxiliary material and adopting the following steps of: selecting and soaking the red dates, crushing the major ingredient to obtain jujube paste, pre-steaming the auxiliary material, fermenting and distilling the major ingredient and the auxiliary material and the like. In the invention, traditional Chinese medicines are also added to the red dates for crushing during the process of crushing the red dates to obtain the jujube paste, wherein the traditional Chinese medicines contain polyphenol acid as an active component; as the traditional Chinese medicines are added for inhibiting the activity of pectin methyl esterase contained in the major ingredient, the purpose of reducing the generation amount of methanol is achieved. The method is simple to operate, is easy to control, and has a good methanol removing effect, and the quality of the spirit product is greatly improved. The method disclosed by the invention is used for brewing the white spirit with data flavor by adopting the red dates as the major ingredient and the bran as the auxiliary material; the content of methanol can be reduced to lower than 0.06%; all indexes of the white spirit product can meet standards of national level I spirit; and the white spirit product has rich jujube fragrance.
Owner:河北万果红酒业有限公司

Extraction tower and process for removing methanol from residual C4 of etherification reaction

The invention relates to an extraction tower and a process for removing methanol from residual C4 of an etherification reaction. The extraction tower comprises a tower body which is internally provided with a plurality of supporting beams; each group of supporting beams corresponds to one layer of tower plate in parallel; a plurality of grooves are formed in each supporting beam at intervals; liquid flow holes communicated with the adjacent lower layer of tower plate are formed in the bottom surfaces of the grooves; each layer of tower plate is formed by splicing a plurality of secondary tower plate pieces; the supporting beams in each two adjacent groups are arranged in a staggered manner; a washing liquid inlet is formed in the upper part of the tower body and a C4 inlet is formed in the lower part of the tower body; a gas-phase outlet is formed in the tower top, and a liquid-phase outlet is formed in the tower bottom. Desalted water which is taken from the outside and has the temperature of 35-45 DEG C enters the tower body from the washing liquid inlet through a desalted water pump, residual C4 of the etherification reaction, which has the temperature of 35-45 DEG C, enters the tower body from the C4 inlet, and the flow ratio of the washing liquid to residual C4 of the etherification reaction is 1 to (20-25). Methanol in mixed C4 with the low methanol content can be removed and the content of methanol in processed mixed C4 is not more than 50ppm so that the consumption amount of a sulfuric acid catalyst in an isooctane device, the energy consumption of the device and the amount of waste acids can be reduced.
Owner:NINGBO HAIYUE NEW MATERIAL

Refrigeration method for methanol synthesis and separation

The invention discloses a refrigeration method for methanol synthesis and separation, and belongs to the technical field of a methanol production process. According to technical essentials of the method, a synthesized gas after a methanol synthetic reaction is subjected to cooling through a heat exchanger and enters an air condenser for further cooling to obtain liquid crude methanol, wax generated in a liquid side reaction, and an un-condensed synthesized gas; a methanol separator is installed after the air condenser to enable wax, generated in the liquid side reaction, together with liquid crude methanol enters the methanol separator and following treatment equipment, so that a total amount of wax entering a following water condenser is reduced, and a wax precipitation speed of the water condenser is reduced; and the un-condensed synthesized gas is subjected to cooling through the heat exchanger and separation through a methanol separating column to enable methanol to be fully condensed and separated, so that the content of methanol in the synthesized gas cycled to a synthetic tower is reduced, and the methanol synthetic reaction in the synthetic tower is promoted to move towards a positive reaction direction. According to the method, the yield of methanol is increased; the service cycle of the device is prolonged; and energy consumption is reduced.
Owner:PETROCHINA CO LTD

Energy-saving methane chloride production system and method

The invention discloses an energy-saving methane chloride production method. The method includes: liquid raw material methanol is heated in a methanol vaporizer, and the methanol is mixed with hydrogen chloride and then enters a reaction kettle through a gas-phase inlet in the lower portion of the reaction kettle; the kettle-bottom produced liquid of the reaction kettle is used as the heating medium of the methanol vaporizer, and the kettle-bottom produced liquid is subjected to heat exchanging through the methanol vaporizer and circulated to a liquid-phase inlet in the upper portion of the reaction kettle; liquid and gas are in continuous countercurrent contact on a tower plate or filler in the reaction kettle; high-temperature mixed gas in the reaction kettle escapes from the top of thereaction kettle, and the gas is cooled by a first condenser and a second condenser and then conveyed to a purification system. The invention further discloses an energy-saving production system used for achieving the method above. The method has the advantages that heat flow produced at the bottom of the reaction kettle and the raw material methanol are subjected to heat exchanging in the methanolvaporizer, the heat carried by the high-temperature heat flow is recycled effectively, reaction heat is utilized sufficiently, all steam needed by methanol preheating and vaporization is saved, and an evident energy saving effect is achieved.
Owner:SEDIN NINGBO ENG

Device and process for recycling methyl alcohol from gas field alcohol-containing sewage based on gas stripping process and vacuum membrane distillation process

The invention relates to a device and a process for recycling methyl alcohol from gas field alcohol-containing sewage based on a gas stripping process and a vacuum membrane distillation process. A complex process route of performing gas stripping first to obtain a dilute methyl alcohol solution with fewer impurities and then concentrating the dilute methyl alcohol solution through vacuum membrane distillation is adopted. The device and the process have the beneficial effects that related equipment such as a complex rectifying tower, a reboiler and a reflux tank is not needed, so that equipment investment is greatly reduced; the integrated process does not generate methyl alcohol reflux, so that repeated heating of reflux and tower bottoms is avoided, raw materials are sufficiently heated by waste heat of a methyl alcohol product and tower bottom water; waste heat of raw materials heated at a gas-stripping section provides energy for phase change of vacuum membrane distillation, so that methyl alcohol recycling energy consumption is greatly reduced and economic benefits are improved; the problems that content of impurities of alcohol-containing sewage of the raw materials is relatively high and the solution pollutes the hydrophobic microporous membrane are avoided, and the service life of the membrane is prolonged; the gas stripping process and the vacuum membrane distillation composite process are integrated, so that recycling efficiency is improved, and content of methyl alcohol in alcohol-containing sewage is reduced.
Owner:CHANGZHOU UNIV

Method for preparing high-purity refined methanol by three-tower rectification

The invention discloses a method for preparing high-purity refined methanol by three-tower rectification, which is used for preparing high-purity refined methanol by treating a methanol crude product by using a three-tower rectification method. The method comprises the steps of: based on diluted alcohol water or soft water as an extraction agent, distilling in a pre-separating tower to remove low-boiling substances in the methanol crude product and water-insoluble gas so as to obtain pre-separated methanol; sending pre-separated methanol into a pressurizing tower for pressurized rectification treatment, cooling light components at the tower top of the pressurizing tower, returning a part of the light components to the tower top of the pressurizing tower for refluxing, and collecting the rest of the light components as the refined methanol product; sending heavy components at the tower bottom of the pressurizing tower into a main rectifying tower for rectification, cooling light components at the tower top of the main rectifying tower, returning a part of the light components to the tower top of the main rectifying tower for refluxing, and collecting the rest of the light components as the refined methanol product; and discharging the main rectifying tower bottom liquid as waste liquid. By using the 'three-tower rectification' method, the problem that methanol azeotropes cannot be separated in the methanol products is effectively solved, the purity of the obtained refined methanol product reaches more than 99.9%, the mass percent concentration of methanol in the discharged waste liquid is smaller than 1.0%, and the pollution of effluents to the environment is reduced because the methanol content is low.
Owner:HUNAN YIHUA CHEM IND
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