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Obtaining Butyl Acetate by the Method of Hydrolysis Nazirova Rakhnamokhon Mukhtarovna; Mirsalimova Saodat Rakhmatjanovna; Isakov Burhon Shuhratjon ogli
International Journal on Orange Technologies Vol. 3 No. 4 (2021): IJOT
Publisher : Research Parks Publishing LLC

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.31149/ijot.v3i4.1601

Abstract

Butyl acetate (butyl ether of acetic acid) is the most common solvent in the production and use of paints and varnishes. Dissolves cellulose ethers, oils, fats, chlorinated rubbers, vinyl polymers, carbiol resins, etc. The addition of butyl acetate together with a small amount of butyl alcohol prevents whitening of the lacquer films. It is a fragrant substance that is part of fruit essences and perfume compositions. It is used in the tanning industry as a tannin. It is widely used in the pharmaceutical industry for the separation of primary substances in the production of antibiotics, etc
Production of NP Fertilizers Based on Local Raw Materials Nazirova Rakhnamokhon Mukhtarovna; Mirsalimova Saodat Rakhmatjanovna; Makhmudov Asror
International Journal on Orange Technologies Vol. 3 No. 4 (2021): IJOT
Publisher : Research Parks Publishing LLC

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.31149/ijot.v3i4.1604

Abstract

Phosphorites S.K are the main phosphate raw materials for the factories of Uzbekistan producing phosphorus-containing fertilizers. The article presents the kinetics of decomposition of phosphorites S.K. sulfuric and extraction phosphoric acids. According to the data obtained, most of the phosphorite (52-65%) decomposes within 10 minutes, and then the process of opening the phosphate is sharply measured. With an equal total rate of acids, an increase in the proportion of sulfuric acid contributes to a deeper decomposition of phosphate. For 3 hours of interaction, an increase in the amount of sulfuric acid contributes to an increase in the degree of opening of the fossil raw material from 83.9 to 90.1%, at a process temperature of 80 ° C at 90 ° C from 89.8 to 93%.