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Autoclavation

Prepared by heating p-nitrochlorobenzene with concentrated aqueous ammonia in an autoclave at 170°C. It is also prepared by alkaline hydrolysis of p-nitroacetanilide or by nitrating and hydrolysing benzylideneaniline. [Pg.276]

On a laboratory scale, hydrotliennal syntliesis is usually carried out in Teflon-coated, stainless-steel autoclaves under autogenous pressure. A typical syntliesis mixture consists of up to four major constituents, a T-atoni source (silicon and aluminium, otlier elements may also be incoriiorated as indicated above), a solvent (almost exclusively... [Pg.2784]

The use of more complex or more costly articles of equipment, such as catalytic hydrogenation apparatus, autoclaves, polari-meters, ultraviolet absorption spectrometers, etc., has not been described, because the type of such apparatus employed indifferent laboratories varies considerably, and students must be taught the use of their own laboratory equipment. [Pg.586]

Secondary and tertiary amines are not generally prepared in the laboratory. On the technical scale methylaniline is prepared by heating a mixture of aniline hydrochloride (55 parts) and methyl alcohol (16 parts) at 120° in an autoclave. For dimethylaniline, aniline and methyl alcohol are mixed in the proportion of 80 78, 8 parts of concentrated sulphuric acid are added and the mixture heated in an autoclave at 230-235° and a pressure of 25-30 atmospheres. Ethyl- and diethyl-anihne are prepared similarly. One method of isolating pure methyl- or ethyl-aniline from the commercial product consists in converting it into the Y-nitroso derivative with nitrous acid, followed by reduction of the nitroso compound with tin and hydrochloric acid ... [Pg.562]

An excellent high pressure autoclave is illustrated in Fig. F7, 4 2. The special feature of this apparatus, constructed almost entirely of... [Pg.868]

Hydrogenations with coppcr-chromium oxide catalyst are usually carried out in the liquid phase in stainless steel autoclaves at pressures up to 5000-6000 lb. per square inch. A solvent is not usually necessary for hydrogenation of an ester at 250° since the original ester and the alcohol or glycol produced serve as the reaction medium. However, when dealing with small quantities and also at temperatures below 200° a solvent is desirable this may be methyl alcohol, ethyi alcohol, dioxan or methylcyc/ohexane. [Pg.872]

The original pressure should not be more than 2,000 lb. per sq. in. if the maximum working pressure for the autoclave is 5,000 lb. The full operating pressure is not applied at the beginning because the pressure will rise as the bomb is heated thus at 256°, the pressure will be 1 - 8 times that at 20°. [Pg.874]

Alizarin. Dissolve successively in 75 ml. of water 6 g. of potassium chlorate, 20 g. of sodium anthraquinone- p-sulphonate and 75 g. of sodium hydroxide. Transfer the mixture to a 500 ml. autoclave (compare Section VI,4) and heat for 20 hours at 170°. After coohng, scrape out... [Pg.981]

Polyamides from diamines and dibasic acids. The polyamides formed from abphatic diamines (ethylene- to decamethylene-diamine) and abphatic dibasic acids (oxabc to sebacic acid) possess the unusual property of forming strong fibres. By suitable treatment, the fibres may be obtained quite elastic and tough, and retain a high wet strength. These prpperties render them important from the commercial point of view polyamides of this type are cabed nylons The Nylon of commerce (a 66 Nylon, named after number of carbon atoms in the two components) is prepared by heating adipic acid and hexamethylenediamine in an autoclave ... [Pg.1019]

This catalyst should really be purchased rather than made because its use in underground chemistry is limited and is hardly watched at all if not ever. This may change considering its potential as a precursor to the NaBHsCN in Strike s 1 method of choice. There are a lot of ways to make this catalyst, but the least involved is the one using boron trifluoride. What the method calls for is an apparatus called an autoclave. You know how using a vacuum causes the absence of pressure to make things boil at a lower temperature Well, an autoclave is a device that causes an... [Pg.279]

Grignard reagent comes from the substitution products it gives with various reactive substrates. When the low-temperature adduct is heated in an autoclave at 90 to 170 C for 3 to 6 hr, it does not rearrange to 2-ethylthiazole (12) as is the case in the pyridine series (436). [Pg.119]

Polycarbonates are the toughest of all thermoplastics. They are window-clear, amazingly strong and rigid, autoclavable, and nontoxic. They have a brittleness temperature of — 135°C. [Pg.1019]

Its key properties are its excellent transparency, rigidity, and chemical resistance, plus its resistance to impact and to high temperatures. It withstands repeated autoclaving, even at 150°C. [Pg.1020]

Polypropylene is translucent and autoclavable and has no known solvent at room temperature. It is slightly more susceptible to strong oxidizing agents than polyethylene. [Pg.1021]

The isopropylidene linkage imparts chemical resistance, the ether linkage imparts temperature resistance, and the sulfone linkage imparts impact strength. The brittleness temperature of polysulfones is — 100°C. Polysulfones are clear, strong, nontoxic, and virtually unbreakable. They do not hydrolyze during autoclaving and are resistant to acids, bases, aqueous solutions, aliphatic hydrocarbons, and alcohols. [Pg.1024]

This compound is sometimes called a nylon salt. The salt polymer equilibrium is more favorable to the production of polymer than in the case of polyesters, so this reaction is often carried out in a sealed tube or autoclave at about 200°C until a fairly high extent of reaction is reached then the temperature is raised and the water driven off to attain the high molecular weight polymer. [Pg.306]

Autoclave tape Autodoping AUTOFLEX Autofrettage Autogenousmilling Autograft... [Pg.79]

Vinyl ethers and a,P unsaturated carbonyl compounds cyclize in a hetero-Diels-Alder reaction when heated together in an autoclave with small amounts of hydroquinone added to inhibit polymerisation. Acrolein gives 3,4-dihydro-2-methoxy-2JT-pyran (234,235), which can easily be hydrolysed to glutaraldehyde (236) or hydrogenated to 1,5-pentanediol (237). With 2-meth5lene-l,3-dicarbonyl compounds the reaction is nearly quantitative (238). [Pg.115]

Crimp. The tow is usually relaxed at this point. Relaxation is essential because it gready reduces the tendency for fibrillation and increases the dimensional stabiUty of the fiber. Relaxation also increases fiber elongation and improves dye diffusion rates. This relaxation can be done in-line on Superba equipment or in batches in an autoclave. Generally saturated steam is used because the moisture reduces the process temperatures required. Fiber shrinkage during relaxation ranges from 10 to 40% depending on the temperature used, the polymer composition used for the fiber, and the amount of prior orientation and relaxation. The amount of relaxation is also tailored to the intended apphcation of the fiber product. [Pg.282]

An alternative hexafluorobenzene process features exchange fluorination (KF) of hexachlorobenzene in the presence of polar solvents (226,249) or under solvent-free conditions (450—540°C, autoclave) (250). Intermediates such as chloropentafluorobenzene can be further fluorinated to hexafluorobenzene (42—51% yield) by cesium fluoride in sulfolane (226,249). [Pg.328]

Trifluoromethylpyridine can be prepared ia 25—65% yield from nicotinic acid and sulfur tetrafluoride (434,439). An alternative method is the passage of chlorine iato a mixture of ( -picoline and hydrogen fluoride ia an autoclave (190°C, 3 MPa) (440). 4-Trifluoromethylpyridine is prepared ia 57% yield from isonicotinic acid and sulfur tetrafluoride. [Pg.338]

Tetrafluoropyrimidine has been prepared by direct fluoriaation of 2,4,6-trifluoropyriniidine with silver difluoride ia perfluorobutylamiae solveat (461,462). A more direct route (85% yield) is the reactioa of tetrachloropyriaiidiae and potassium fluoride ia an autoclave at 480°C for 42 h (463). [Pg.340]

Chloro-2,4,6-trifluoropyrimidine [697-83-6] has gained commercial importance for the production of fiber-reactive dyes (465,466). It can be manufactured by partial fluoriaation of 2,3,5,6-tetrachloropyrimidine [1780-40-1] with anhydrous hydrogen fluoride (autoclave or vapor phase) (467) or sodium fluoride (autoclave, 300°C) (468). 5-Chloro-2,4,6-trifluoropyrimidine is condensed with amine chromophores to provide the... [Pg.340]


See other pages where Autoclavation is mentioned: [Pg.47]    [Pg.170]    [Pg.433]    [Pg.1957]    [Pg.2767]    [Pg.568]    [Pg.868]    [Pg.869]    [Pg.873]    [Pg.924]    [Pg.106]    [Pg.280]    [Pg.26]    [Pg.146]    [Pg.95]    [Pg.79]    [Pg.79]    [Pg.38]    [Pg.141]    [Pg.232]    [Pg.233]    [Pg.8]    [Pg.180]    [Pg.486]    [Pg.307]    [Pg.330]    [Pg.340]   
See also in sourсe #XX -- [ Pg.91 , Pg.93 ]




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Aerated concretes, autoclaved

Agitated mini-autoclaves

Antigen Retrieval on Thin Resin Sections Using Autoclaving

Applications to Autoclave Curing

Autoclave (Steam Sterilizer)

Autoclave (pressure cooker)

Autoclave (stirred tank

Autoclave Autoclaving

Autoclave Autoclaving

Autoclave Buildup

Autoclave Free-volume

Autoclave INDEX

Autoclave Molding of Graphite Epoxy Composites

Autoclave Processing (AP)

Autoclave Processing Description

Autoclave Vulcanisation

Autoclave bonding

Autoclave chamber

Autoclave cleaning

Autoclave cleaning tests

Autoclave containment facility

Autoclave cure

Autoclave cure cycle

Autoclave curing, VARTM

Autoclave development

Autoclave dimensional control

Autoclave experiments, methods

Autoclave flow compaction

Autoclave forming

Autoclave future trends

Autoclave gradients

Autoclave gypsum

Autoclave heat setting

Autoclave history

Autoclave indicators

Autoclave laboratory clothing

Autoclave leaching

Autoclave method

Autoclave model

Autoclave molding

Autoclave molding operation

Autoclave molds

Autoclave moulding

Autoclave moulding (prepreg)

Autoclave nitrogen atmosphere

Autoclave performance qualification

Autoclave performances, comparison

Autoclave press clave

Autoclave press claves

Autoclave process

Autoclave process development

Autoclave process tooling

Autoclave processing for composites

Autoclave production

Autoclave products

Autoclave qualification

Autoclave reaction

Autoclave reactors

Autoclave rooms

Autoclave safety requirements

Autoclave schematic

Autoclave set

Autoclave steaming

Autoclave sterilization

Autoclave stirring

Autoclave stresses

Autoclave synthesis

Autoclave technique

Autoclave technology

Autoclave temperature development

Autoclave testing

Autoclave tests

Autoclave tests described

Autoclave thermal expansion

Autoclave thermal strains

Autoclave to VARTM

Autoclave tool removal process

Autoclave tooling

Autoclave treatment

Autoclave typical cycle

Autoclave typical system

Autoclave use of hydrogenation bomb

Autoclave venting

Autoclave vulcanization

Autoclave waste decontamination

Autoclave work, batch

Autoclave, equipment sterilization

Autoclave, internally heated

Autoclave, internally heated measurements

Autoclave, shaking

Autoclave, slurried hydrogenation

Autoclave-induced reaction

Autoclaved

Autoclaved calcium silicate hydrates

Autoclaved lime

Autoclaved materials

Autoclaved materials very high strength

Autoclaves

Autoclaves

Autoclaves AIRTC

Autoclaves and Sterilizers

Autoclaves and autoclaving

Autoclaves curing

Autoclaves double ended

Autoclaves high vacuum

Autoclaves pressures

Autoclaves problems

Autoclaves processing

Autoclaves, agitated

Autoclaves, hydrothermal synthesis

Autoclaves, validation

Autoclaving

Autoclaving

Autoclaving and Sterile Preparation

Autoclaving epitope retrieval with

Autoclaving method

Autoclaving moist

Autoclaving temperatures

Autoclaving validation

Autoclaving, instruments

Basic chemistry of autoclave processes

Batch autoclave reactor, catalytic

Boiling under pressure (Kiering in autoclaves)

Bulk polymerization autoclave

CATALYTIC HYDROGENATION AUTOCLAVES

Cell-autoclave reactor

Cement autoclaved

Cement paste autoclaved

Commercial Parr autoclave

Composite materials autoclave process

Concrete autoclave aerated

Contact time autoclaves

Continuous autoclave reactor

Corrosion from autoclaves

Curing autoclave moldings

Drying autoclave

Effluent autoclave

Equipment (Autoclaves, etc

Equipment autoclave

Glass autoclaving

Heating methods autoclave

Hydrogenation autoclaves

Hydrogenation bomb, use of, as autoclave

Infrared autoclave

Injectable products autoclaving

LDPE Autoclave Reactor

LDPE autoclave process

Lamination, autoclave

Lamination, autoclave Orientation process

Liquid crystals high-pressure autoclave

Metallurgy autoclaving

Micro-autoclave

Out of autoclave processes

Out-of-autoclave curing process

Out-of-autoclave curing process (Cont processes

Out-of-autoclave curing process in polymer matrix composites

Parr autoclave

Polyethylene autoclave

Polymer matrix composites autoclave processing

Polymerization reactor autoclave-type

Polyolefin autoclave reactor

Pressure equipment autoclave bonding

Processing autoclave molding

Pyrrhotite from autoclaves

Reactor 1 Agitated Mini-autoclaves

Reinforced-plastic autoclave molding

Resin sections autoclaving

Rotating autoclave

Safety autoclaves

Saturated steam autoclaves

Saturated steam autoclaves construction

Saturated steam autoclaves process

Sealed autoclave

Silica autoclave curing

Spinning-falling basket autoclaves

Steam autoclave

Sterile autoclaved) broth

Sterilisation processes autoclaving

Superheated water spray autoclaves

The Autoclave Process

Thermal insulation materials, autoclaved

Toroid cavity autoclave

Washer/autoclaves

Waste autoclaving

Water-autoclave

Water-autoclave extraction

Water-autoclave extracts

Water-autoclave procedure

Wet autoclave method

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