Production of Higher Alcohols with Minimum Methanol Content from the Gasification of Carbonaceous Materials
US-2015361015-A1 · Dec 17, 2015 · US
US2019202763A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2019202763-A1 |
| Application number | US-201716311909-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 21, 2017 |
| Priority date | Jun 21, 2016 |
| Publication date | Jul 4, 2019 |
| Grant date | — |
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A device for manufacturing an organic substance, including: a synthesis gas generation unit for generating a synthesis gas; an impurity concentration reducing unit including an adsorbent which is capable of adsorbing impurities contained in the synthesis gas, and produces a purified gas by contact of the adsorbent with the synthesis gas; an organic substance synthesis unit for producing an organic substance-containing solution from the purified gas as a raw material; an extraction unit for extracting the organic substance by heating the organic substance-containing solution; a heating unit for preparing heated gas to be fed to the adsorbent; and a heat supplying unit which supplies the extraction unit with heat of the heated gas fed from the heating unit to the adsorbent.
Opening claim text (preview).
1 . A device for manufacturing an organic substance, comprising: a synthesis gas generation unit for generating a synthesis gas; an impurity concentration reducing unit comprising an adsorbent which is capable of adsorbing impurities contained in the synthesis gas, and produces a purified gas by contact of the adsorbent with the synthesis gas; an organic substance synthesis unit for producing an organic substance-containing solution from the purified gas as a raw material; an extraction unit for extracting the organic substance by heating the organic substance-containing solution; a heating unit for preparing heated gas to be fed to the adsorbent; and a heat supplying unit which supplies the extraction unit with heat of the heated gas fed from the heating unit to the adsorbent. 2 . The device according to claim 1 , wherein the organic substance-containing solution contains water, and the organic substance is ethanol. 3 . The device according to claim 1 , wherein the extraction unit comprises a distillation device. 4 . The device according to claim 3 , wherein the distillation device is a multi-effect distillation device. 5 . The device according to claim 1 , wherein the heat supplying unit has a heat exchanger. 6 . The device according to claim 1 , wherein the synthesis gas generation unit has a device for partially oxidizing a carbon source to generate a synthesis gas containing carbon monoxide and an impurity. 7 . The device according to claim 6 , wherein the impurity is at least one compound selected from the group consisting of benzene, toluene, ethylbenzene, and xylene. 8 . A method for manufacturing an organic substance, comprising: a synthesis gas generation step of generating a synthesis gas; an impurity concentration reducing step of contacting the synthesis gas with an adsorbent capable of adsorbing impurities contained in the synthesis gas, thereby reducing an impurity concentration of the synthesis gas to obtain a purified gas; an organic substance synthesis step of producing an organic substance-containing solution from the purified gas as a raw material; and an extraction step of extracting the organic substance by heating the organic substance-containing solution, wherein the method further comprises a desorption step of bringing a heated gas into contact with the adsorbent used in the impurity concentration reducing step to desorb impurities from the adsorbent, and wherein heat of the heated gas having gone through the desorption step is recovered and reused in the extraction step. 9 . The method according to claim 8 , wherein the extraction step is a step of distilling the organic substance-containing solution.
Cooling or heating systems · CPC title
Pressure swing adsorption · CPC title
by absorption · CPC title
by treating with solids; Regenerating spent purifying masses {(separation by adsorption B01D53/02; separation by chemical reaction B01D53/34; refining of hydrocarbon oils with acids C10G17/02, C10G27/02, C10G29/12)} · CPC title
Multiple effect distillation · CPC title
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