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Stirred continuous

Place 50 g. of o-chloronitrobenzene and 75 g. of clean dry sand in a 250 ml. flask equipped with a mechanical stirrer. Heat the mixture in an oil or fusible metal bath to 215-225° and add, during 40 minutes, 50 g. of copper bronze or, better, of activated copper bronze (Section 11,50, 4) (1), Maintain the temperature at 215-225° for a further 90 minutes and stir continuously. Pour the hot mixture into a Pyrex beaker containing 125 g. of sand and stir until small lumps are formed if the reaction mixture is allowed to cool in the flask, it will set to a hard mass, which can only be removed by breaking the flask. Break up the small lumps by powdering in a mortar, and boil them for 10 minutes with two 400 ml. [Pg.527]

Method 2. In a 500 ml. round-bottomed flask, equipped with a reflux condenser, place 20 5 g. (20 ml.) of anUine, 21 5 g. (20 ml.) of acetic anhydride, 21 g. (20 ml.) of glacial acetic acid, and 01 g. of zinc dust (1), Boil the mixture gently for 30 minutes, and then pour the hot Uquid in a thin stream into a 1 Utre beaker containing 500 ml. of cold water whilst stirring continually. When cold (it is preferable to cool in ice), filter the crude product at the pump, wash with a Uttle cold water, drain well and dry upon filter paper in the air. The yield of acetaniUde, m.p. 113°, is 30 g. It may be recrystaUised as in Method 1 aflFording 21 g, of pure acetaniUde, m.p. 114°. [Pg.577]

To 40 g. of dry chitin in a 500-ml. beaker is added 200 ml. of concentrated hydrochloric acid (c.p., sp. gr. 1.18), and the mixture is heated on a boiling water bath for 2.5 hours with continuous mechanical agitation. At the end of this time solution is complete, and 200 ml. of water and 4 g. of Norite are added. The beaker is transferred to a hot plate, and the solution is maintained at a temperature of about 60° and is stirred continuously during the process of decolorization. After an hour the solution is filtered through a layer of a filter aid such as Filter-Cel. The filtrate is usually a pale straw color however, if an excessive color persists, the decolorization may be repeated until the solution becomes almost colorless. The filtrate is concentrated under diminished pressure at 50° until the volume of the solution is 10-15 ml. The white crystals of glucosamine hydrochloride are... [Pg.36]

Potassium biiodate [13455-24-8] M 389.9. Crystd three times from hot water (3mL/g), stirred continuously during each cooling. After drying at 100° for several hours, the crystals are suitable for use in volumetric analysis. [Pg.453]

In a 3-I. round-bottomed, three-necked flask fltted with a liquid-sealed mechanical stirrer, a thermometer, and a 500-cc. separatory funnel are placed 1700 cc. of dry ben2ene and 160 g. (1.2 moles) of powdered, anhydrous aluminum chloride (Note i). The mixture is cooled to 10° by means of an ice-water bath and maintained at 10-20 during the addition of a solution of 120 g. (0.58 mole) of benzalacetophenone (Note 2) (Org. Syn. Coll. Vol. I, 71) in 300 cc. of dry benzene. This addition requires about thirty minutes. The cooling bath is then removed and stirring continued at room temperature until all the dense, yellow precipitate formed at first has gone into solution (Note 3). The reaction is complete after stirring for an additional hour. [Pg.51]

A solution of 7.2 g of sodium borohydride (analyzing at 87 % purity) in 300 ml of pyridine is added dropwise, with vigorous stirring, over 7 hr to a solution of 50 g of pregnane-3,11,20-trione in 100 ml of pyridine and 18 ml of water. The temperature is kept at 18-20°. The stirring at this temperature is continued for another 2 hr, after which the reaction mixture is poured slowly into dilute hydrochloric acid (575 ml of cone hydrochloric acid in 5.2 liters of water) and the stirring continued for 1 hr. The precipitate is filtered, washed with... [Pg.92]

The rhodium catalyst (46 mg) is dissolved in acetone (10 ml) in a microhydrogenation apparatus which is then flushed three times with deuterium gas. After stirring the solution in an atmosphere of deuterium for about 1 hr the deuterium uptake ceases and constant pressure is attained. 5a-Cholest-2-ene (136, 19.5 mg) is added and the stirring continued until deuterium uptake ceases (about 3/4 hr). The solvent is evaporated to dryness and the residue is extracted with hexane and the resulting solution filtered through a small alumina column (3 g, activity 111). Evaporation of the hexane gives 2, 3 -d2-5oc-cholestane (137) 18 mg, 92% mp 78-79° isotope composition 94%d2,5%d, andl%do. ... [Pg.188]

B) Acylation of 6-Aminopenicillanic Acid To a solution of the aryl halocarbonyl ketene (0.1 mol) in methylene chloride (sufficient to provide a clear solution and generally from about 5 to 10 ml per gram of ketene) there is added the proper alcohol RjOH (0.1 mol), in this case 5-indanyl alcohol. The reaction mixture is maintained under an atmosphere of nitrogen and stirred for a period of from 20 minutes to 3 hours, care being taken to exclude moisture. The temperature may range from about -70° to about -20°C. The infrared spectrum of the mixture is then taken to determine and confirm the presence of the ketene ester. A solution of 6-aminopenicillanic acid-triethylamine salt (0.1 mol) in methylene chloride (50 ml) is added and the mixture stirred at -70° to -20°C for 10 minutes. The cooling bath is then removed and the reaction mixture stirred continuously and allowed to warm to room temperature. [Pg.237]

Stage 4 Preparation of 1-l2-Phenyi-2-Methoxyl -Ethyi-4-[3-Phenyl-3-Hydroxypropyl] -Piperazine Dihydrochioride - In a double-neck flask equipped with a thermometer and a mechanical stirrer, there is placed in suspension in 800 ml of methanol, 233 grams of 1-[2-phenyl-2-methoxy]-ethyl-4-[2-benzoyl-ethyl]-piperazine dihydrochioride (0.55 mol). It is cooled to approximately 5°C, and 46 grams of NaOH pellets dissolved in 80 ml of HjO are added. When the temperature is about 5°C, one addition of 29,2 grams of sodium borohydride in 40 ml HjO is made. The ice-bath is then removed and stirring continued at ambient temperature for 6 hours. [Pg.567]

Chlorine gas was gradually passed into 660 parts of benzene contained in a lead-lined reaction vessel until 890 parts of the gas had been absorbed. The mixture was stirred continuously and the temperature maintained at 15°C to 20°C. [Pg.879]

A solution of 32 g (030 mol) phosgene in 200 ml benzene is added dropwise at 30°C to a stirred soiution of 53.5 g (032 mol) 3-o-toloxy-13-Pfopanediol in 400 ml benzene. The mixture is stirred for an hour after the addition is completed, and a solution of 39 g of dl-methylaniline in 100 ml benzene is then added, and stirring continued for a half-hour. Ice water (about one-third volume) is then added, and the benzene layer formed is separated and stirred with 500 ml concentrated ammonia at 5°Cfor six hours. The precipitated solid (weighing about 55 g) is recovered and recrystallized from water. The product thus obtained in a yield of about 53 g is 3-(o-toloxy)-2-hydroxypropyl carbamate it is a crystalline solid melting at about 93°C, and having a lower water-solubility and higher oil-solubility than 3-o-toloxy-13-propanediol. [Pg.935]

To the aqueous suspension of the palladized charcoal catalyst thus obtained are added 20.8 kg of 3-cyano-pyridine (96% purity) and then are added 70 liters of a hydrochloric acid solution prepared by diluting 30 liters of 36% HCI with 40 liters of water. This represents approximately 1.75 mols of HCI for each mol of 3-cyano-pyridine. The suspension is maintained at 10° to 15°C and stirred continuously while introducing a current of hydrogen at a pressure of 3 to 5 psi. When absorption of hydrogen ceases and the 3-cyano-pyridine is completely reduced, the reaction mixture is filtered to remove the catalyst. [Pg.1075]

To a batch of approximately 10 liters of filtered broth is added 150 grams of activated charcoal. The mixture is stirred continuously for about 5 minutes and is then filtered. [Pg.1393]

N-Acetylation of Kasugamycinic Acid (9a). A solution of kasugamycinic acid (225 mg.) dissolved in 10 ml. of water was treated with acetic anhydride (0.3 ml.) under cooling sodium bicarbonate was used to keep the pH 7.2 and stirring continued for 30 minutes. The reaction product was passed through Dowex 50W-X2 (H form) and the column was washed with water. The combined filtrate was subjected to lyophilization to afford 234 mg. of a crude N-acetyl derivative. Its infrared spectrum showed strong absorptions at 1740 cm-1 characteristic of oxamic acid group. The N-acetyl derivative (178 mg.) was treated with 40 ml. [Pg.43]

Preparation ofpure potassium hydrogeniodate. Dissolve 27 g of potassium iodate in 125 mL of boiling water, and add a solution of 22 g of iodic acid in 45 mL of warm water acidified with six drops of concentrated hydrochloric acid. Potassium hydrogeniodate separates on cooling. Filter on a sintered-glass funnel, and wash with cold water. Recrystallise three times from hot water use 3 parts of water for 1 part of the salt and stir continuously during each cooling. Dry the crystals at 100 °C for several hours. The purity exceeds 99.95 per cent. [Pg.294]

Add cautiously (FUME CUPBOARD), and with constant stirring, 10 mL of the ammonium citrate solution this will prevent the precipitation of metals when, at a later stage, the pH value of the solution is increased. Then add 10 mL of the 20 percent ascorbic acid, and adjust to pH 4(BDH narrow-range indicator paper), by the cautious addition of concentrated ammonia solution down the side of the beaker while stirring continuously. Then add lOmL of the 50 per cent potassium cyanide solution (CAUTION ) and immediately adjust to a PH of 9-10 (BDH indicator paper) by the addition of concentrated ammonia solution. [Pg.809]

Jha and Bhowmick [51] have reported the development and properties of thermoplastic elastomeric blends from poly(ethylene terephthalate) and ACM by solution-blending technique. For the preparation of the blend the two components, i.e., poly(ethylene terephthalate) and ACM, were dried first in vacuum oven. The ACM was dissolved in nitrobenzene solvent at room temperature with occasional stirring for about three days to obtain homogeneous solution. PET was dissolved in nitrobenzene at 160°C for 30 min and the rubber solution was then added to it with constant stirring. The mixture was stirred continuously at 160°C for about 30 min. The blend was then drip precipitated from cold petroleum ether with stirring. The ratio of the petroleum ether/nitrobenzene was kept at 7 1. The precipitated polymer was then filtered, washed with petroleum ether to remove nitrobenzene, and then dried at 100°C in vacuum. [Pg.111]

The mixed solution obtained was then placed in a syringe and allowed to drop into a sterile 0.2M CaCli solution that was stirred continuously. Alginate drops solidified upon contact with CaCh, forming beads and thus entrapping bacteria cells. The beads were allowed to harden for 30 minutes at 37 C and then washed with sterile saline solution to remove excess calcium ions and untrapped cells. [Pg.406]


See other pages where Stirred continuous is mentioned: [Pg.625]    [Pg.879]    [Pg.945]    [Pg.118]    [Pg.120]    [Pg.79]    [Pg.148]    [Pg.1187]    [Pg.423]    [Pg.8]    [Pg.108]    [Pg.6]    [Pg.478]    [Pg.74]    [Pg.304]    [Pg.253]    [Pg.288]    [Pg.984]    [Pg.1394]    [Pg.95]    [Pg.45]    [Pg.465]    [Pg.526]    [Pg.607]    [Pg.623]    [Pg.907]    [Pg.37]    [Pg.823]    [Pg.63]    [Pg.15]    [Pg.559]    [Pg.46]    [Pg.47]   
See also in sourсe #XX -- [ Pg.16 , Pg.163 , Pg.174 , Pg.180 , Pg.181 , Pg.189 ]




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Adiabatic continuous flow stirred tank reactors

Anaerobic reactor, continuous flow stirred

B Concentration Response in a Continuous Stirred Tank with Chemical Reaction

Batch and Continuous Stirred Tank Reactors

Batch continuous stirred tanks

Biochemical reactors Continuous stirred-tank reactor

Bioreactor continuous stirred

Bioreactors continuous stirred-tank reactor

C Constant-Volume Continuous Stirred-Tank Reactor

CONTINUOUS STIRRED TANK

CSTR (continuous stirred-tank

CSTR - Continuous Stirred-Tank Cascade

CSTR dynamics Continuous stirred tank reactors

CSTRPULSE - Continuous Stirred-Tanks, Tracer Experiment

CSTR—See Continuous stirred

CSTR—See Continuous-stirred tank

CSTR—See Continuous-stirred tank reactor

Cascading, continuous stirred tank reactors

Case A Continuous Stirred-Tank Reactor (CSTR)

Case A. Continuous Stirred-Tank Reactor

Catalytic continuous flow stirred tank reactors

Catalytic reactor, continuously-stirred

Cell continuous stirred-tank fermentor

Cell continuous stirred-tank fermentors

Chaotic dynamics continuous stirred tank reactor

Constant-volume continuous stirred tank

Constant-volume continuous stirred tank reactor

Continuous Stirred Tank Reactor The Adiabatic Case

Continuous Stirred Tank Reactor The Nonadiabatic Case

Continuous Stirred Tank and the Plug Flow Reactors

Continuous Stirred-Tank Fermentor

Continuous Stirred-Tank Reactors (General Treatment)

Continuous Stirred-tank Fermenter (CSTF)

Continuous fermentation stirred tank fermenters

Continuous flow reactors continuously stirred tank

Continuous flow stirred tank reactor

Continuous flow stirred tank reactor CFSTR)

Continuous flow stirred tank reactors CSTR)

Continuous flow stirred tank reactors defined

Continuous flow, well stirred tank reactor

Continuous ideally stirred tank reactor

Continuous ideally stirred tank reactor CISTR)

Continuous operated stirred tank reactor

Continuous operation stirred tank-CSTR

Continuous stirred membrane

Continuous stirred membrane bioreactors

Continuous stirred reactor

Continuous stirred reactor oscillations

Continuous stirred reactor parallel reactions

Continuous stirred reactor periodic states

Continuous stirred tank crystallizer

Continuous stirred tank reactor

Continuous stirred tank reactor (CSTR batch recycle

Continuous stirred tank reactor (CSTR cascade

Continuous stirred tank reactor CSTR) polymerization

Continuous stirred tank reactor CSTR) tests

Continuous stirred tank reactor Contribution

Continuous stirred tank reactor See

Continuous stirred tank reactor adiabatic

Continuous stirred tank reactor autothermal operation

Continuous stirred tank reactor cascaded

Continuous stirred tank reactor component balance

Continuous stirred tank reactor consecutive reactions

Continuous stirred tank reactor endothermic

Continuous stirred tank reactor energy balance

Continuous stirred tank reactor equilibrium reactions

Continuous stirred tank reactor feed temperature

Continuous stirred tank reactor hysteresis

Continuous stirred tank reactor isothermal reactions

Continuous stirred tank reactor linearization

Continuous stirred tank reactor mass balance

Continuous stirred tank reactor material balance

Continuous stirred tank reactor mathematics

Continuous stirred tank reactor model

Continuous stirred tank reactor nonlinear equations

Continuous stirred tank reactor operating points

Continuous stirred tank reactor ordinary differential equations

Continuous stirred tank reactor population balance

Continuous stirred tank reactor process

Continuous stirred tank reactor recycle

Continuous stirred tank reactor residence time

Continuous stirred tank reactor simulation

Continuous stirred tank reactor space time

Continuous stirred tank reactor space velocity

Continuous stirred tank reactor stability

Continuous stirred tank reactor steady-state multiplicity

Continuous stirred tank reactor temperature

Continuous stirred tank reactor terms

Continuous stirred tank reactor tubular

Continuous stirred tank reactor with heat transfer

Continuous stirred tank reactor with recycle

Continuous stirred tank reactors agitators/impellers

Continuous stirred tank reactors control system

Continuous stirred tank reactors in series

Continuous stirred tank reactors performance

Continuous stirred tank reactors, kinetic data

Continuous stirred tank separator

Continuous stirred tank separator CSTS)

Continuous stirred tank, 165 equation

Continuous stirred ultrafiltration

Continuous stirred-tank bioreactor

Continuous stirred-tank bioreactor CSTB)

Continuous stirred-tank cascade tracer experiment

Continuous stirred-tank extraction

Continuous stirred-tank extractor

Continuous stirred-tank reactor CSTR)

Continuous stirred-tank reactor latex from

Continuous stirred-tank reactor mathematical model

Continuous stirred-tank reactor nonisothermal

Continuous stirred-tank reactor system

Continuous stirred-tank reactor weight distribution

Continuous stirred-tank reactors (CSTRs

Continuous stirred-tank reactors multiple steady states

Continuous stirred-tank-reactor cascades

Continuous stirring tank reactor

Continuous well-stirred extractor

Continuous-flow stirred tank

Continuous-flow stirred tank electrochemical reactor

Continuous-stirred lank reactors

Continuous-stirred tank reactors adiabatic operation

Continuous-stirred tank reactors design equation

Continuous-stirred tank reactors residence-time distribution

Continuous-stirred tank reactors space

Continuous-stirred-tank reactor, mass

Continuous-stirred-tank reactor, mass transfer model

Continuously Stirred Tank Reactor...See CSTR

Continuously fed stirred-tank reactor

Continuously operated stirred tank

Continuously operated stirred tank reactor

Continuously operated stirred tank reactor CSTR)

Continuously stirred reactor membrane bioreactor

Continuously stirred tank

Continuously stirred tank reactor

Continuously stirred tank reactor CSTR)

Continuously stirred tank reactor cascades

Continuously stirred tank reactor describing equations

Continuously stirred tank reactor model

Continuously stirred tank reactor operation

Continuously stirred tank reactor semi-batch reactors

Continuously stirred tank reactor unsteady state operations

Continuously-stirred tank catalytic

Conversion rate, continuous stirred tank reactor

Copolymerization, continuous stirred

Copolymerization, continuous stirred tank reactor

Design equation ideal continuous stirred tank

Design equations for continuous stirred-tank reactors

Design of Continuous Stirred Tank Reactors (CSTRs

Dynamics of a Continuous Stirred Tank Reactor

Enzyme reactors continuous-stirred

Enzymes continuous stirred tank reactor

Example Continuous Stirred Tank Reactor

Exercise 11.1 Mixing in a continuous stirred tank reactor

Experimental continuous flow stirred tank reactor

Fermentor continuous stirred-tank fermentors

First continuous stirred-tank reactor

Flow regime Continuously stirred tank reactor

Fluidized continuous-stirred tank reactors

Gas-liquid continuous-stirred tank

Homogeneous continuous stirred tank

Homogeneous continuous stirred tank reactor

Homogeneous continuous stirred tank reactor HCSTR)

Ideal Continuous Stirred Tank Reactor (CSTR)

Ideal Continuously Operated Stirred Tank Reactor (CSTR)

Ideal continuous stirred tank reactor

Ideal reactors continuously stirred tank reactor

Ideal reactors, continuously stirred tank reactor liquid phase reaction

Ideal reactors, continuously stirred tank reactor residence time

Ideal reactors, continuously stirred tank reactor series

Ideal reactors, continuously stirred tank reactor steady state

Kinetic data from continuous stirred-tank reactors

Material balance Ideal continuous stirred tank

Michaelis continuous stirred-tank reactor

Model 2 The Ideal Continuous Stirred Tank Reactor (CSTR) with V Constant

Modeling continuous stirred tank reactor,

Modelling a Continuous Stirred Tank Reactor (CSTR)

Multi-stage continuous flow stirred tank

Multi-stage continuous flow stirred tank reactor

Multiple Stationary States in Continuous Stirred Tank Reactors

Multiplicity, continuous stirred tank

Multiplicity, continuous stirred tank reactor

Multistationarity in kinetic models of continuous flow stirred tank reactors

Nonisothermal CSTR Continuous stirred tank reactors

Oscillations, continuous flow stirred

Oscillations, continuous flow stirred tank reactors

Plug-flow reactor and single continuous stirred tank

Polyethylene continuous stirred-tank reactor

Polymerization reactions continuous flow stirred

Polymerization reactor continuous-stirred tank

Precipitators continuous stirred tank reactors

Propagation rate, continuous stirred

Propagation rate, continuous stirred tank reactor

Reactivity ratios continuous stirred tank

Reactor continuously stirred

Reactor models continuous well-stirred model

Reactor, batch continuous flow stirred tank

Reactors continuously stirred tank batch

Reactors continuously stirred tank plug-flow

Reactors continuously stirred tank semi-batch

Reactors continuously stirred tank tubular

Reactors, chemical stirred tanks, batch and continuous

Segregated CSTR Continuous stirred tank reactors

Self-heating in a continuous stirred tank reactor

Semi continuous stirred tanks

Single continuous stirred tank and two tanks in series

Solution polymerization continuous flow stirred

Stage Continuous Flow Stirred Tank Reactor

Stationary Conditions for a Nonisothermal Continuous Stirred Tank Reactor

Steady State of a Continuous Stirred-Tank Reactor

Steady state conditions continuous stirred tank

Steady state continuously stirred tank

Stirred Tanks with a Continuous Polymer Phase

Stirred continuous flow

Stirred continuous mode

Stirred continuous reactor cascades

Stirred-tank continuous mode

Styrene continuous flow stirred

The Continuous Flow Stirred Tank Reactor

The Continuous Stirred-Tank Reactor

The Continuous-Stirred-Tank Reactor (CSTR)

The Ideal Continuous Flow Stirred-Tank Reactor

Tracer continuous-stirred tank reactor

Transient Continuous Stirred Tank Reactors

Transient continuously stirred

Vinyl acetate polymerization continuous stirred tank reactor

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