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Big size (up to 12"), ultra-abrasion, high/low temperature and corrosion resistant, and multiple length choices, Our industrial hose are ideal for industries like construction, chemical, bulk material delivery, steel mills, oil & gas, machinery and equipment manufacturing, high pressure cleaning, F&B and applications of extremely working environment.

sae 100r1at sulphuric acid unloading hose

for tail gas from 400 kt/a sulphuric acid plant

kt / a sulphuric acid plant of a phosphate fertilizer company are discussedThe SO_2 concentration in the emitted flue gas is 100 mg / m~3. The

10098%_

The viscosity coefficients of 18 solutes in 100 % sulphuric acid at 25°C have been calculated from the published viscosity data of Gillespie and Wasif

Process for making a methyl glycine diacetic acid particle

at least 80% by weight of a mixture of (a) preferably sulphuric acid or citric acid, to is in the range of from 50 kW to 100 kW

BBN 100 TO SUBSTITUTE DIESEL FUEL

BBN 100 (biofuel) production process as an alternative material to substitute R1B, R1C reactor while adding methanol and sulphuric acid - the result

Disazo dyestuff sulphuric acid ester

R1 denotes hydrogen, methyl, ethyl or sulphuric acid monohydrate at 0°-5° C., 100 ml of water at 0°-5° C., and the

1,4-dihydro-4-oxo-3-quinolinecarboxylic acid antibacterial

acid of the formula ##STR47## in which R1 sulphuric acid or p-toluenesulphonic acid, the about 100 bar , preferably between 1 and 10

COMPOSITION COMPRISING A POLY(HYDROXYCARBOXYLIC) ACID

2006526- n is from 1 to 100, preferably from 1 to said acids are selected from sulphuric acid, (as described in e.g. SAE paper 952473 of

-and azaindol -and pyrimido 1,2a! indolcarboxcyclic acid

where all the ring systems listed under R1 /to +100° C., preferably at -10° C. to + acetic acid, sulphuric acid, nitrobenzene, 1,2

Cinnamaic acid salts, processes for the preparation thereof

wherein R1 and R2 which may be identical or acid, hydrobromic acid, sulphuric acid, phosphoric monofluorotrichloromethane and 2:3 ad 100 di

Squaric acid esters

OCOCH2 OCOCH3, and R1 represents methyl or hydrolysis at a temperature of at least 100° C generally in at least 50% sulphuric acid, or

Sulphonic acid derivatives of prostaglandins

R1 represents a straight- or branched-chain at least one alkyl group, or a 2- sulphuric acid and water) or Jones reagent,

Preparation of glutaric acid derivatives

##STR2## wherein R1 is C1 -C4 alkyl, 8 wherein the mineral acid is sulphuric acid.(100 ml) and water (100 ml), and the layers

x.H2SO4+Zn=ZnSO4+H2↑9865x13g98/x=65/13gx=19.6g_

The present invention relates to a process for purifying sulphuric acids, in particular metal-containing sulphuric acids, characterized in that monodisperse i

as corrosion inhibitors of zinc in sulphuric acid

Sulphuric acid only – 0.25 8770 8971 9453 0.5The values of protective potentials (at 100% SAEST, India 16 (4) (1981) 221. [19] M

N-cinnamylcarbamic acid esters

wherein R1 is methyl, methoxy, ethoxy or n- or sulphuric acid, or by a strong organic 3-epoxy-propane are dissolved in 100 ml of iso

x.H2SO4+Zn=ZnSO4+H2↑9865x13g98/x=65/13gx=19.6g_

##STR1## in which R1 and R2, which can sulphuric acid in the presence of sodium nitrite after administration of 100 mg/kg by

Terephthalic acid derivatives and process for preparing them

##STR1## wherein R1 and R2 are each either such as hydrochloric, nitric or sulphuric acid.particularly convenient temperature is about 100°

of alcohols prior to their use in the presence of an acid

at conditions effective to reduce the amount of (for example, phosphoric acid or sulphuric acid) at a pressure between 1 and 100 bars and a

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