Skip to main content

Acetic Acid Manufacturing Process


Reaction
  RAW MATERIAL REQUIREMENT TO MAKE 1 METRIC TON ACETIC ACID
Acetaldehyde                    : 1100 kg
Manganous Acetate       : 3.3 kg
Air                                          : 233 Cubic meter

PROCESS
99-99.8% concentrated Acetaldehyde solution is introduced into a stainless steel Reaction vessel in which air at 70 to 75 psi (480 kPa to 520 kPa) bubbles through the liquid 955 to 65 degree C) which contains 0.1 to 0.5% Manganous Acetate used to decompose the explosive intermediate Peraacetic Acid. In batches 4085 kg Acetaldehyde can be completely Oxidized in 12 hours. The gases leaving the reactor are scrubbed with water, releasing Nitrogen and decomposition products to the Atmosphere. The dilute Acetaldehyde solution leaving the bottom of the scrubber is sent to a column for recovery. The crude Acetic Acid (94 to 96%) is Discharged frm the reactor and continuously rectified to yield 99% Glacial Acetic Acid.
In some modern plants the oxidation is carried out continuously rather than in batches. The catalyst in this case is Cobalt Acetate dissolved in Acetic Acid. The reactor is operated at 15 psi (100 kPa) and 70 to 80 degree C. Approximately 4 moles of air enter the converter per mole of Acetaldehyde.
Conversions of 20 to 30% per pass and yields of 95 to 96% of theory may be obtained. If Oxygen is used in place of Air, the pressure in system may be reduced to 30 psi or 210 kPa and good recovery obtained.
An alternative vapor phase oxidation process currently in use employs a mixture of Alcohol and Acetaldehyde, which on catalytic Air oxidation yields both Acetaldehyde and Acetic acid as products. By recycling the Acetaldehyde, adding only Alcohol to the system as makeup, and removing only Acetic acid, the process becomes essentially a catalytic vapor phase Alcohol oxidation to Acetic acid.
PROPERTIES
(Glacial Acetic acid) Colorless liquid with pungent odor and sharp acid taste.
Molecular Weight            : 60.05
Specific Gravity                 : 1.0492, 20 degree C/4
Weight per gallon            : 8.64 lb (20 degree C)
Melting Point                     : 16.6 degree C
Boiling Point                       : 118.1 degree C
Flash Point (open cup)   : 39 degree C
Ignition Temperature     : 516 degree C
Vapor Density (air = 1)   : 2.07
Explosive Limits % by volume in air           : Lower 6.6 and Upper 19.9
Threshold Limit value in ppm      : 10
Soluble in all proportions with water, ethanol, glycerin, and ether at room temperature. Insoluble in carbon disulfide.
Dangerous fire hazard in contact with chromic acid, sodium peroxide, or nitric acid.
Containers & Regulations – Tank cars, tank trucks, tight barrels, Aluminum drum, carboys, and bottles. Glacial Acetic Acid expands on solidification and may burst the container unless stored at a temperature above 16 degree C. and requires a White DOT shipping label.

Comments

  1. ๐Ÿ™‹๐ŸคŸ๐Ÿ‘ i appreciate your work

    ReplyDelete

Post a Comment

If you have any doubts, please let me know

Popular posts from this blog

CRYSTALLIZER DESIGN CALCULATION

Given Data Solute                                                                    : A Solvent                                                                  : B Concentration of Solute                                  : 0.25 Kg of Solute/Kg of Solvent Temperature                                                      : 50 to 20 O C Maximum allowable growth rate (G)           : 3.0 ยต m/min Product Crystal Size (L p )                                 : 2000 ยต m Available Seed Size (L s )                                   : 100 ยต m Production Rate Crystal (P)                           : 500 Kg Feed Concentration (C o )                               :0.25 Kg A/Kg B Feed Temperature (T o )                                  : 50 O C Density of Feed Solution ( ฯ o )                       : 1.05 Kg/L Density of Mother Liquor ( ฯ f )                      : 1.05 Kg/L Density of Solute Crystal ( ฯ s )                       : 1.8 Kg/L Desired final Temperature (

Sugar Mill Roller Grooves

SUGAR MILL ROLLER GROOVING     The three rolls of a conventional mill are arranged in a triangle so that the fiber is squeezed twice between the top roll and the feed roll and the top roll and the discharge roll. The rolls have cast iron, grooved shells mounted on steel shafts. Fiber passing between the top and feed roll is conducted over a turner plate to the discharge roll. The rolls are pinion driven from the top roll which is driven at a speed of 3 to 6 rpm by a gear reduction system. The feed and discharge rolls are fixed, while the top roll is free to move up and down by means of a hydraulic pressure system. Cane is moved between mills by means of intermediate conveyors. They are generally rake or drag-slat type, which carry the fiber to a fixed chute leading to the next mill. 1)       Circumferential Grooves a)       Cutting grooves around the roll gives a corrugated surface of increased area which has better gripping action because of the compression of

Calcium Carbonate

Calcite                    : CaCO3 Refractive Index         : 1.66-1.74 Specific Gravity         : 2.71 Mohs Hardness          : 3 Aragonite              : CaCO3 Refractive Index        : 1.68-1.69 Specific Gravity        : 2.95 Mohs Hardness         : 3.5-4 The mineral calcite is the major or sole constituent of most commercial calcium carbonate products. These include natural limestone, marble, and chalk, plus most precipitated calcium carbonate. Aragonite is a metastable polymorph of calcite that typically has an acicular crystal shape. Natural aragonite products are less common, but precipitated varieties are available. Many calcium carbonate deposits are the remains of the shells and skeletons of ancient sea life. The color, purity, density, and crystal morphology depend upon the influence of waves and water currents before burial, and upon temperature, pressure, and tectonic activity after burial. The most common mineral impurities are quartz and clay.  The m