摘要:
Disclosed is a process for removing mineral matter from Rundle oil-shale by contacting the oil-shale with (a) an ammonium salt solution and (b) an organic solvent, at a temperature from about 0.degree. C. to about 300.degree. C. for a time which is sufficient to substantially separate at least about 80 wt. % of the carbonate mineral matter from the oil-shale.
摘要:
A process in which organic sulfur, nitrogen and oxygen compounds are essentially quantitatively removed from hydrocarbon feedstocks by contacting said feedstocks with liquid hydrogen fluoride in the presence of hydrogen. Preferred feedstocks are those boiling in the range of from about -185.degree.C to about 345.degree.C wherein the sulfur content ranges from about 0.001 to about 10 wt. %, preferably 0.001 to about 3 wt. %.
摘要:
Methods for separating carbon dioxide from a gas stream are described. The methods include (a) providing a stream having a gas therein; and (b) contacting the stream with a sorption composition thereby removing at least a portion of the gas from the stream. The sorption composition includes a solid support, a linking moiety, and a gas-capture moiety or a reaction product thereof; wherein the gas-capture moiety has a formula according to Formula (I): wherein R1 to R3 may be the same or different and are selected from H or hydrocarbyl (e.g., selected from the group consisting of substituted or unsubstituted, branched or linear C1-C20 alkyl groups and substituted or unsubstituted, branched or linear C1-C20 alkenyl groups); wherein X is selected from the group consisting of H, hydrocarbyl groups, and amino and alkylamino groups,
摘要:
Ionic liquids containing a cation with a potentially nucleophilic carbon atom bearing a relatively acidic hydrogen atom bonded to a potentially nucleophilic carbon atom, typically in the conjugated —NC(H)N— structure or a —NC(H)S— structure of imidazolium, imidazolidinium or thiazolium salts, can be capable of acting as sorbents for CO2 in cyclic separation processes. The ionic liquid may be used on its own, mixed with a solvent, preferably an aprotic, polar, non-aqueous solvent such as toluene, DMSO, NMP or sulfolane, or in conjunction with a non-nucleophilic nitrogenous base promoter compound having a pKa of at least 10.0 such as a carboxamidine or a guanidine.
摘要:
A process for increasing the selectivity of an alkanolamine absorption process for selectively removing hydrogen sulfide (H2S) from a gas mixture which also contains carbon dioxide (CO2) and possibly other acidic gases such as COS, HCN, CS2 and sulfur derivatives of C1 to C4 hydrocarbons, comprises contacting the gas mixture with a liquid absorbent which is a severely sterically hindered capped alkanolamine or more basic sterically hindered secondary and tertiary amine. The improvement in selectivity is achieved at the high(er) pressures, typically least about 10 bara at conditions nearing the H2S/CO2 equilibrium at which CO2 begins to displace absorbed hydrosulfide species from the absorbent solution.
摘要翻译:提高烷醇胺吸收方法选择性地从还含有二氧化碳(CO 2)和可能的其它酸性气体如COS,HCN,CS2和C1至C4的硫衍生物的气体混合物中除去硫化氢(H 2 S)的选择性的方法 烃类包括使气体混合物与液体吸收剂接触,液体吸收剂是严格位阻封端的链烷醇胺或更基本的空间位阻的仲胺和叔胺。 在接近H2S / CO 2平衡的条件下,在高(呃)压力下,通常至少约10巴,实现了选择性的改善,在该平衡下,CO 2开始从吸收剂溶液中置换吸收的氢硫化物物质。
摘要:
Promoter amines are used to enhance CO2 uptake by sterically hindered or tertiary amines. The promoter amines can be cyclic amines, including aromatic cyclic amines or bridged cyclic amines. The combination of a promoter amine plus a sterically hindered or tertiary amines allows for improved uptake kinetics while reducing or minimizing the amount of formation of carbamate salts. The promoted sterically hindered or tertiary amines can be used as part of a CO2 capture and release system that involves a phase transition from a solution of amine-CO2 products to a slurry of amine-CO2 precipitate solids.
摘要:
Systems and methods are provided for performing CO2 sorption and regeneration processes that can take advantage of phase changes between solutions of amine-CO2 reaction products and precipitate slurries, where the slurry particles can include solid precipitates formed based on the amine-CO2 reaction products. An amine solution can be used to capture CO2 from a gas phase stream. During this initial capture process, the amine-CO2 reaction product can remain in solution. The solution containing the amine-CO2 reaction product can then be exposed to a set of conditions which result in precipitation of a portion of the amine-CO2 reaction product to form a slurry. The precipitate slurry can be passed into one or more release stages where the conditions for the slurry are altered to allow for release of the CO2.
摘要:
An acid gas absorbent comprising an alkylamino alkyloxy (alcohol) monoalkyl ether and a process for the selective removal Of H2S from gaseous mixtures containing H2S and CO2 using an absorbent solution comprising an alkylamino alkyloxy alcohol monoalkyl ether.
摘要:
An acid gas absorbent comprising a metal sulfonate, phosphonate or carboxylate of a hindered amine and a process for the selective removal Of H2S as well as other acidic components such as carbon disulfide, carbonyl sulfide and oxygen and sulfur derivatives of C1 to C4 hydrocarbons from mixtures containing such acidic components and CO2 using said absorbent.
摘要:
The feeding of coal slurries into a gasifier for the production of synthesis gas is improved by modifying the rheological properties of the coal particles so that conventional liquid transfer equipment can be used in the feed transfer process to the gasifier. The coal particle surface modification is accomplished by adsorbing asphaltenes derived from petroleum onto the surfaces of coal particles prior to and/or during contact with the slurry liquid. The coal particles with their surfaces thus modified exhibit lower particle-particle interaction in the liquid slurries to form a shear independent Newtonian fluid or a weakly shear thickening pseudoplastic fluid. The rheological properties of the slurries permit them to be transported reliably into a pressurized, entrained feed gasifier vessel using convention slurry pumps with a low potential expenditure of energy.