Carbon dioxide quenching

Treatment of 33 with two equivalents of sec-butyllithium in the presence of tetramethylethylenediamine (TMEDA) at -70°C with gradual warming to -45°C, followed by a carbon dioxide quench at -70°C and acidification afforded the acid 23 in 62% yield. 

The saturated, cleaned raw synthesis gas from a Texaco partial oxidation system is first shifted by use of a sulfur resistant catalyst. Steam required for shifting is already present ia the gas by way of the quench operation ia the generator. The shifted gas is then processed for hydrogen sulfide and carbon dioxide removal followed by Hquid nitrogen scmbbiag. 

The reactor effluent is rapidly quenched with aqueous mother Hquor in specially designed equipment operating at pressures essentially equal to the reactor pressure. This operation yields an off-gas consisting of ammonia and carbon dioxide vapor and a crystalline melamine slurry saturated with ammonia and carbon dioxide. The slurry is concentrated in a cyclone mill. The mother Hquor overflow is returned to the quenching system. The concentrated slurry is redissolved in the mother Hquor of the crystallization system, and the dissolved ammonia is stripped simultaneously. 

This ammonia is recycled to the reactor via a compressor and a heater. Liquid ammonia is used as reflux on the top of the absorber. The net amount of carbon dioxide formed in the reactor is removed as bottom product from the absorber in the form of a weak ammonium carbamate solution, which is concentrated in a desorber-washing column system. The bottom product of this washing column is a concentrated ammonium carbamate solution which is reprocessed in a urea plant. The top product, pure ammonia, is Hquefted and used as reflux together with Hquid makeup ammonia. The desorber bottom product, practically pure water, is used in the quench system in addition to the recycled mother Hquor. 

In a typical gas oil design, the lighter products overhead from the quench tower/primary fractionator are compressed to 210 psi, and cooled to about 100°F. Some Q plus material is recovered from the compressor knockout drums. The gases are ethanolamine and caustic washed to remove acid gases sulfur compounds and carbon dioxide, and then desiccant dried to remove last traces of water. This is to prevent ice and hydrate formation in the low temperamre section downstream. 

The in situ generation of the carbon dioxide adduct of an indole provides sufficient protection and activation of an indole for metalation at C-2 with r-butyl-lithium. The lithium reagent can be quenched with an electrophile, and quenching of the reaction with water releases the carbon dioxide. ... 

To a solution of 516 nig (1 mmol) of the stannane 17 (R = C.H3, 95% ee) in 10 ml of dry DME is added, at — 78 C, 0.62 nlL of 1.6 M BuLi (1 mmol) in hexane. After 5 min gaseous carbon dioxide is bubbled into ihe yellow solution. The reaction mixture decolorizes immediately. After a further 10 min the reaction is quenched with sat. aq NH4C1. The organic layer is extracted with 2N aq NaOll. Acidification of the aqueous layer with 2N aq IICI is followed by extraction with F.t,o, drying over Na,SC)4 and concentration in vacuo yield 193 mg (92%) 95% ec [determined by HPLC-analysis of the amide obtained by derivati/alion with (S)-x-phenylelhylaminc] [a]20 — 37 (r = 1,6, CI1C1,). 

The stereochemistry of the carboxylation of 4-substituted ( + )-(/ S)-fra ,v-1-(4-mcthylphcnyl-sulfinylmethyl)cyclohexane after metalation with methyllithium and quenching with carbon dioxide was reported64. The results listed in Table 1 show that the d.r. of around 75 25 under kinetic control changes to 25 75 under thermodynamic control. This is the result of the equilibration of the two diastereomeric metalated species. As shown by the experiment in hexamethylphosphoric Iriamide (IIMI A) (d.r. = 57 43 under kinetic control) an electrophilic assistance of the lithium cation to the electrophilic approach is probably involved. 

By quenching the polymerization with C1402 or Cl40 the determination of the number of propagation rate constants was found to be also possible for the two-component catalytic system TiCl2 + AlEt2Cl 158, 159). In contrast to alcohols, carbon dioxide and carbon monoxide under polymerization conditions react only with titanium-carbon active bonds and do not react with inactive aluminum-polymer bonds. 

The product, calcium hydroxide, is commonly known as slaked lime because, as calcium hydroxide, the thirst of lime for water has been quenched (slaked). Slaked lime is the form in which lime is normally sold because quicklime can set fire to moist wood and paper. In fact, the wooden boats that were once used to transport quicklime sometimes caught fire in the heat of reaction when water seeped into their holds. An aqueous solution of calcium hydroxide, which is slightly soluble in water, is called lime water. It is used as a test for carbon dioxide, with which it reacts to form a suspension of the much less soluble calcium carbonate ... 

Both oxidative and non-oxidative routes with similar share are followed, yielding hydrogen or water as additional products. As by-products, carbon dioxide and carbon monoxide, methyl formate and formic acid are generated. It is advised to quench the exit stream as formaldehyde decomposition can occur. 

From the quench scrubber (B) the gas passes to an absorption column (C) in which the acrylonitrile is absorbed in water to produce a 3 wt per cent solution. The carbon dioxide, unreacted propylene, oxygen, nitrogen and unreacted hydrocarbons are not absorbed and are vented to atmosphere from the top of column (C). 

Allenamide ( )-13 was prepared by trapping the corresponding lithioallene with carbon dioxide, followed by conversion of the carboxylate to the amide. Chromatographic resolution of the enantiomers of 13 was easily accomplished on a 10x250mm Chiralcel OD HPLC column. Addition of vinyllithium 14 to (+)-13, followed by quenching the reaction with aqueous NaH2P04, led to cyclopentenone (—)-15 in 64% yield with >95% chirality transfer (Eq. 13.4). The absolute stereochemistry of (-)-5 is consistent with the mechanistic hypothesis put forth in Eq. 13.3 [8]. 

This type of system may be used for the extinguishment of surface fires in flammable liquids, gases, and solids where the hazard is not enclosed. Examples of hazards that may be successfully protected by local application systems include dip tanks, quench tanks, and spray booths. Since local application systems do not utilize enclosures to maintain design concentrations, two methods for determining the quantity of carbon dioxide required for extinguishment are used. These are ... 

Two traditional methods have been used to Introduce a carboxyl substituent at C-5 of uracil. 0ns iasolves bromlnatlon at C-5, metalatlon via a lithium-halogen exchange, and finally quenching with carbon dioxide (32) to give the C-5 carboxylic acid. The... 

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