20 research outputs found
Wave roller research on barley crops
A completely new design of the wave roller is presented, which has no analogues produced by the industry. As a result of research on barley crops, it was revealed that the optimization criterion kse after treatment with the developed wave roller is 0.81. The density and aggregate composition of the soil in all parts of the field (in the ridges and in the troughs of the wave relief) fully meets the agrotechnical requirements. In the area after treatment with a serial roller KKZ-6, the optimization criterion kse = 0.67, which is significantly lower than that of the proposed wave roller. At the same time, soil clods were found on the soil surface, the size of which exceeds 50 mm, which does not meet the agrotechnical requirements for rolling. Studies conducted under production conditions made it possible to determine that the rolling of barley crops with the proposed wave roller increased its yield to 47.2 centners per hectare (by 12.4%) compared to 42 centners per hectare after rolling the crops with ring-toothed rollers KKZ-6
Ancient origin, functional conservation and fast evolution of DNA-dependent RNA polymerase III
RNA polymerase III contains seventeen subunits in yeasts (Saccharomyces cerevisiae and Schizosaccharomyces pombe) and in human cells. Twelve of them are akin to the core RNA polymerase I or II. The five other are RNA polymerase III-specific and form the functionally distinct groups Rpc31-Rpc34-Rpc82 and Rpc37-Rpc53. Currently sequenced eukaryotic genomes revealed significant homology to these seventeen subunits in Fungi, Animals, Plants and Amoebozoans. Except for subunit Rpc31, this also extended to the much more distantly related genomes of Alveolates and Excavates, indicating that the complex subunit organization of RNA polymerase III emerged at a very early stage of eukaryotic evolution. The Sch.pombe subunits were expressed in S.cerevisiae null mutants and tested for growth. Ten core subunits showed heterospecific complementation, but the two largest catalytic subunits (Rpc1 and Rpc2) and all five RNA polymerase III-specific subunits (Rpc82, Rpc53, Rpc37, Rpc34 and Rpc31) were non-functional. Three highly conserved RNA polymerase III-specific domains were found in the twelve-subunit core structure. They correspond to the Rpc17-Rpc25 dimer, involved in transcription initiation, to an N-terminal domain of the largest subunit Rpc1 important to anchor Rpc31, Rpc34 and Rpc82, and to a C-terminal domain of Rpc1 that presumably holds Rpc37, Rpc53 and their Rpc11 partner
Cooperation between Translating Ribosomes and RNA Polymerase in Transcription
International audienceDuring transcription of protein-coding genes, bacterial RNA polymerase (RNAP) is closely followed by a ribosome that translates the newly synthesized transcript. Our in vivo measurements show that the overall elongation rate of transcription is tightly controlled by the rate of translation. Acceleration and deceleration of a ribosome result in corresponding changes in the speed of RNAP. Moreover, we found an inverse correlation between the number of rare codons in a gene, which delay ribosome progression, and the rate of transcription. The stimulating effect of a ribosome on RNAP is achieved by preventing its spontaneous backtracking, which enhances the pace and also facilitates readthrough of roadblocks in vivo. Such a cooperative mechanism ensures that the transcriptional yield is always adjusted to translational needs at different genes and under various growth conditions
The Human Isoform of RNA Polymerase II Subunit hRPB11bΞ± Specifically Interacts with Transcription Factor ATF4
Rpb11 subunit of RNA polymerase II of Eukaryotes is related to N-terminal domain of eubacterial α subunit and forms a complex with Rpb3 subunit analogous to prokaryotic α2 homodimer, which is involved in RNA polymerase assembly and promoter recognition. In humans, a POLR2J gene family has been identified that potentially encodes several hRPB11 proteins differing mainly in their short C-terminal regions. The functions of the different human specific isoforms are still mainly unknown. To further characterize the minor human specific isoform of RNA polymerase II subunit hRPB11bα, the only one from hRPB11 (POLR2J) homologues that can replace its yeast counterpart in vivo, we used it as bait in a yeast two-hybrid screening of a human fetal brain cDNA library. By this analysis and subsequent co-purification assay in vitro, we identified transcription factor ATF4 as a prominent partner of the minor RNA polymerase II (RNAP II) subunit hRPB11bα. We demonstrated that the hRPB11bα interacts with leucine b-Zip domain located on the C-terminal part of ATF4. Overexpression of ATF4 activated the reporter more than 10-fold whereas co-transfection of hRPB11bα resulted in a 2.5-fold enhancement of ATF4 activation. Our data indicate that the mode of interaction of human RNAP II main (containing major for of hRPB11 subunit) and minor (containing hRPB11bα isoform of POLR2J subunit) transcription enzymes with ATF4 is certainly different in the two complexes involving hRPB3–ATF4 (not hRPB11a–ATF4) and hRpb11bα–ATF4 platforms in the first and the second case, respectively. The interaction of hRPB11bα and ATF4 appears to be necessary for the activation of RNA polymerase II containing the minor isoform of the hRPB11 subunit (POLR2J) on gene promoters regulated by this transcription factor. ATF4 activates transcription by directly contacting RNA polymerase II in the region of the heterodimer of α-like subunits (Rpb3–Rpb11) without involving a Mediator, which provides fast and highly effective activation of transcription of the desired genes. In RNA polymerase II of Homo sapiens that contains plural isoforms of the subunit hRPB11 (POLR2J), the strength of the hRPB11–ATF4 interaction appeared to be isoform-specific, providing the first functional distinction between the previously discovered human forms of the Rpb11 subunit
Wave roller research on barley crops
A completely new design of the wave roller is presented, which has no analogues produced by the industry. As a result of research on barley crops, it was revealed that the optimization criterion kse after treatment with the developed wave roller is 0.81. The density and aggregate composition of the soil in all parts of the field (in the ridges and in the troughs of the wave relief) fully meets the agrotechnical requirements. In the area after treatment with a serial roller KKZ-6, the optimization criterion kse = 0.67, which is significantly lower than that of the proposed wave roller. At the same time, soil clods were found on the soil surface, the size of which exceeds 50 mm, which does not meet the agrotechnical requirements for rolling. Studies conducted under production conditions made it possible to determine that the rolling of barley crops with the proposed wave roller increased its yield to 47.2 centners per hectare (by 12.4%) compared to 42 centners per hectare after rolling the crops with ring-toothed rollers KKZ-6
Technology and Properties
ΠΠ΅ΡΡΡΠ½ΠΎΠΉ ΠΊΠΎΠΊΡ - ΠΎΡΠ½ΠΎΠ²Π½ΠΎΠ΅ ΡΡΡΡΠ΅ Π΄Π»Ρ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π°Π½ΠΎΠ΄ΠΎΠ² Π°Π»ΡΠΌΠΈΠ½ΠΈΠ΅Π²ΡΡ
ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΠ·Π΅ΡΠΎΠ².
ΠΠ°ΡΠ΅ΡΡΠ²ΠΎ ΠΊΠΎΠΊΡΠ° Π²ΠΎ ΠΌΠ½ΠΎΠ³ΠΎΠΌ ΠΎΠΏΡΠ΅Π΄Π΅Π»ΡΠ΅Ρ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΡ, ΡΠΊΠΎΠ»ΠΎΠ³ΠΈΡ ΠΈ ΡΠΊΠΎΠ½ΠΎΠΌΠΈΠΊΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π°Π»ΡΠΌΠΈΠ½ΠΈΡ.
Π‘ ΡΠΎΡΠΊΠΈ Π·ΡΠ΅Π½ΠΈΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΠΈΡΠ΅Π»Π΅ΠΉ Π°Π»ΡΠΌΠΈΠ½ΠΈΡ, Π½Π΅ΡΡΡΠ½ΠΎΠΉ ΠΊΠΎΠΊΡ Π΄ΠΎΠ»ΠΆΠ΅Π½ ΠΎΠ±Π»Π°Π΄Π°ΡΡ ΡΠ»Π΅Π΄ΡΡΡΠΈΠΌΠΈ
ΡΠ²ΠΎΠΉΡΡΠ²Π°ΠΌΠΈ: ΠΌΠΈΠ½ΠΈΠΌΠ°Π»ΡΠ½ΠΎΠΉ Π·ΠΎΠ»ΡΠ½ΠΎΡΡΡΡ ΠΈ ΠΎΡΡΡΡΡΡΠ²ΠΈΠ΅ΠΌ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΡΠΈΠΌΠ΅ΡΠ΅ΠΉ, Π²ΡΡΠΎΠΊΠΎΠΉ
ΡΡΠΎΠΉΠΊΠΎΡΡΡΡ ΠΊ ΠΊΠΈΡΠ»ΠΎΡΠΎΠ΄Ρ ΠΈ Π‘Π2, Π½ΠΈΠ·ΠΊΠΎΠΉ ΠΏΠΎΡΠΈΡΡΠΎΡΡΡΡ ΠΈ ΡΠ΄Π΅Π»ΡΠ½ΡΠΌ ΡΠ»Π΅ΠΊΡΡΠΎΡΠΎΠΏΡΠΎΡΠΈΠ²Π»Π΅Π½ΠΈΠ΅ΠΌ,
ΠΌΠ΅Ρ
Π°Π½ΠΈΡΠ΅ΡΠΊΠΎΠΉ ΠΏΡΠΎΡΠ½ΠΎΡΡΡΡ, ΠΏΡΠΈΠ΅ΠΌΠ»Π΅ΠΌΠΎΠΉ Π΄Π»Ρ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠΈ, ΠΈ Ρ
ΠΎΡΠΎΡΠ΅ΠΉ ΠΌΠΈΠΊΡΠΎΡΡΡΡΠΊΡΡΡΠΎΠΉ.
ΠΠ΅ΡΡΡΠ½ΠΎΠΉ ΠΊΠΎΠΊΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡ ΠΈΠ· ΠΎΡΡΠ°ΡΠΊΠΎΠ² ΠΏΠ΅ΡΠ΅ΡΠ°Π±ΠΎΡΠΊΠΈ Π½Π΅ΡΡΠΈ ΠΈ Π²ΡΠΎΡΠΈΡΠ½ΡΡ
Π½Π΅ΡΡΠ΅ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ².
Π ΡΠΈΠ»Ρ ΠΎΡΠΎΠ±Π΅Π½Π½ΠΎΡΡΠ΅ΠΉ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΠΈ ΠΊΠ°ΡΠ΅ΡΡΠ²ΠΎ Π½Π΅ΡΡΡΠ½ΠΎΠ³ΠΎ ΠΊΠΎΠΊΡΠ° ΡΠ²Π»ΡΠ΅ΡΡΡ ΠΊΠΎΠΌΠΏΡΠΎΠΌΠΈΡΡΠΎΠΌ ΠΌΠ΅ΠΆΠ΄Ρ
ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΠ΅ΠΌ ΡΠ²Π΅ΡΠ»ΡΡ
Π½Π΅ΡΡΠ΅ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ² ΠΈ ΡΡΡΡΡ Π΄Π»Ρ ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΡ. ΠΠΎΡΡΠΎΠΌΡ Π½Π΅ΡΠ΄ΠΈΠ²ΠΈΡΠ΅Π»ΡΠ½ΠΎ, ΡΡΠΎ
ΠΎΡΠ΅Π½Ρ Π½Π΅Π±ΠΎΠ»ΡΡΠΎΠ΅ ΠΊΠΎΠ»ΠΈΡΠ΅ΡΡΠ²ΠΎ ΠΊΠΎΠΊΡΠΎΠ² ΠΌΠΎΠ³ΡΡ ΡΠ΄ΠΎΠ²Π»Π΅ΡΠ²ΠΎΡΠΈΡΡ Π²ΡΠ΅ΠΌ ΡΡΠ΅Π±ΠΎΠ²Π°Π½ΠΈΡΠΌ Π°Π»ΡΠΌΠΈΠ½ΠΈΠ΅Π²ΠΎΠΉ
ΠΏΡΠΎΠΌΡΡΠ»Π΅Π½Π½ΠΎΡΡΠΈ. Π ΡΡΠ°ΡΡΠ΅ Ρ ΡΠΎΡΠΊΠΈ Π·ΡΠ΅Π½ΠΈΡ ΠΌΠΈΡΠΎΠ²ΠΎΠ³ΠΎ ΠΎΠΏΡΡΠ° Π°Π»ΡΠΌΠΈΠ½ΠΈΠ΅Π²ΠΎΠΉ ΠΏΡΠΎΠΌΡΡΠ»Π΅Π½Π½ΠΎΡΡΠΈ
ΡΠ°ΡΡΠΌΠΎΡΡΠ΅Π½Ρ Π²ΠΎΠΏΡΠΎΡΡ ΡΠΎΡΠΌΠΈΡΠΎΠ²Π°Π½ΠΈΡ ΡΠ²ΠΎΠΉΡΡΠ² ΠΊΠΎΠΊΡΠ° ΠΎΡ Π½Π°ΡΠ°Π»Π° Π½Π΅ΡΡΠ΅ΠΏΠ΅ΡΠ΅ΡΠ°Π±ΠΎΡΠΊΠΈ Π΄ΠΎ ΡΠΊΠ»Π°Π΄Π°
ΡΡΡΡΡ Π°Π½ΠΎΠ΄Π½ΠΎΠ³ΠΎ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π°. ΠΡΠ΅Π΄Π»Π°Π³Π°Π΅ΠΌΠ°Ρ ΡΡΠ°ΡΡΡ ΡΠ²Π»ΡΠ΅ΡΡΡ ΠΏΠ΅ΡΠ²ΠΎΠΉ Π² ΡΠ΅ΡΠΈΠΈ ΡΠΎΠ²ΠΌΠ΅ΡΡΠ½ΡΡ
ΡΠ°Π±ΠΎΡ ΡΠΎΡΡΡΠ΄Π½ΠΈΠΊΠΎΠ² Π‘ΠΈΠ±ΠΈΡΡΠΊΠΎΠ³ΠΎ ΡΠ΅Π΄Π΅ΡΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΡΠ½ΠΈΠ²Π΅ΡΡΠΈΡΠ΅ΡΠ° ΠΈ ΡΠΏΠ΅ΡΠΈΠ°Π»ΠΈΡΡΠΎΠ² ΠΡΠΈΠ½ΡΠΊΠΎΠ³ΠΎ ΠΠΠ,
ΠΏΠΎΡΠ²ΡΡΠ΅Π½Π½ΡΡ
ΡΡΡΠΎΠΈΡΠ΅Π»ΡΡΡΠ²Ρ ΠΈ ΡΠ°Π·Π²ΠΈΡΠΈΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π½Π΅ΡΡΡΠ½ΠΎΠ³ΠΎ ΠΊΠΎΠΊΡΠ° Π½Π° ΠΡΠΈΠ½ΡΠΊΠΎΠΌ ΠΠΠ.Petroleum coke is the main raw material for aluminum electrolysis anodes. Quality of coke determinates
the technology, ecology and economics of production of aluminum. From the aluminum producers
point of view, petroleum coke should have the following characteristics:
- a minimum ash content and the absence of impurities,
- high resistance to oxygen and CO2,
- low porosity and electrical resistivity
- mechanical strength, acceptable for processing
- good microstructure.
Petroleum coke is produced from petroleum residues and secondary petroleum products. Because of
the peculiarity of the technology, the quality of petroleum coke is a compromise between the receipt of
light fuel and raw coking. It is not surprising that only a very small amount of coke can satisfy all the
requirements of the aluminum industry. The purpose this article is formation of cokes properties from
the beginning of oil refining up to the anode plant. The article is the first in a lot of cooperated works
of the Siberian Federal University and specialists of the Achinsk refinery, dedicated to construction
and development of production of petroleum coke at the Achinsk refinery
Technology and Properties
ΠΠ΅ΡΡΡΠ½ΠΎΠΉ ΠΊΠΎΠΊΡ - ΠΎΡΠ½ΠΎΠ²Π½ΠΎΠ΅ ΡΡΡΡΠ΅ Π΄Π»Ρ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π°Π½ΠΎΠ΄ΠΎΠ² Π°Π»ΡΠΌΠΈΠ½ΠΈΠ΅Π²ΡΡ
ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΠ·Π΅ΡΠΎΠ².
ΠΠ°ΡΠ΅ΡΡΠ²ΠΎ ΠΊΠΎΠΊΡΠ° Π²ΠΎ ΠΌΠ½ΠΎΠ³ΠΎΠΌ ΠΎΠΏΡΠ΅Π΄Π΅Π»ΡΠ΅Ρ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΡ, ΡΠΊΠΎΠ»ΠΎΠ³ΠΈΡ ΠΈ ΡΠΊΠΎΠ½ΠΎΠΌΠΈΠΊΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π°Π»ΡΠΌΠΈΠ½ΠΈΡ.
Π‘ ΡΠΎΡΠΊΠΈ Π·ΡΠ΅Π½ΠΈΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΠΈΡΠ΅Π»Π΅ΠΉ Π°Π»ΡΠΌΠΈΠ½ΠΈΡ, Π½Π΅ΡΡΡΠ½ΠΎΠΉ ΠΊΠΎΠΊΡ Π΄ΠΎΠ»ΠΆΠ΅Π½ ΠΎΠ±Π»Π°Π΄Π°ΡΡ ΡΠ»Π΅Π΄ΡΡΡΠΈΠΌΠΈ
ΡΠ²ΠΎΠΉΡΡΠ²Π°ΠΌΠΈ: ΠΌΠΈΠ½ΠΈΠΌΠ°Π»ΡΠ½ΠΎΠΉ Π·ΠΎΠ»ΡΠ½ΠΎΡΡΡΡ ΠΈ ΠΎΡΡΡΡΡΡΠ²ΠΈΠ΅ΠΌ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΡΠΈΠΌΠ΅ΡΠ΅ΠΉ, Π²ΡΡΠΎΠΊΠΎΠΉ
ΡΡΠΎΠΉΠΊΠΎΡΡΡΡ ΠΊ ΠΊΠΈΡΠ»ΠΎΡΠΎΠ΄Ρ ΠΈ Π‘Π2, Π½ΠΈΠ·ΠΊΠΎΠΉ ΠΏΠΎΡΠΈΡΡΠΎΡΡΡΡ ΠΈ ΡΠ΄Π΅Π»ΡΠ½ΡΠΌ ΡΠ»Π΅ΠΊΡΡΠΎΡΠΎΠΏΡΠΎΡΠΈΠ²Π»Π΅Π½ΠΈΠ΅ΠΌ,
ΠΌΠ΅Ρ
Π°Π½ΠΈΡΠ΅ΡΠΊΠΎΠΉ ΠΏΡΠΎΡΠ½ΠΎΡΡΡΡ, ΠΏΡΠΈΠ΅ΠΌΠ»Π΅ΠΌΠΎΠΉ Π΄Π»Ρ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠΈ, ΠΈ Ρ
ΠΎΡΠΎΡΠ΅ΠΉ ΠΌΠΈΠΊΡΠΎΡΡΡΡΠΊΡΡΡΠΎΠΉ.
ΠΠ΅ΡΡΡΠ½ΠΎΠΉ ΠΊΠΎΠΊΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡ ΠΈΠ· ΠΎΡΡΠ°ΡΠΊΠΎΠ² ΠΏΠ΅ΡΠ΅ΡΠ°Π±ΠΎΡΠΊΠΈ Π½Π΅ΡΡΠΈ ΠΈ Π²ΡΠΎΡΠΈΡΠ½ΡΡ
Π½Π΅ΡΡΠ΅ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ².
Π ΡΠΈΠ»Ρ ΠΎΡΠΎΠ±Π΅Π½Π½ΠΎΡΡΠ΅ΠΉ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΠΈ ΠΊΠ°ΡΠ΅ΡΡΠ²ΠΎ Π½Π΅ΡΡΡΠ½ΠΎΠ³ΠΎ ΠΊΠΎΠΊΡΠ° ΡΠ²Π»ΡΠ΅ΡΡΡ ΠΊΠΎΠΌΠΏΡΠΎΠΌΠΈΡΡΠΎΠΌ ΠΌΠ΅ΠΆΠ΄Ρ
ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΠ΅ΠΌ ΡΠ²Π΅ΡΠ»ΡΡ
Π½Π΅ΡΡΠ΅ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ² ΠΈ ΡΡΡΡΡ Π΄Π»Ρ ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΡ. ΠΠΎΡΡΠΎΠΌΡ Π½Π΅ΡΠ΄ΠΈΠ²ΠΈΡΠ΅Π»ΡΠ½ΠΎ, ΡΡΠΎ
ΠΎΡΠ΅Π½Ρ Π½Π΅Π±ΠΎΠ»ΡΡΠΎΠ΅ ΠΊΠΎΠ»ΠΈΡΠ΅ΡΡΠ²ΠΎ ΠΊΠΎΠΊΡΠΎΠ² ΠΌΠΎΠ³ΡΡ ΡΠ΄ΠΎΠ²Π»Π΅ΡΠ²ΠΎΡΠΈΡΡ Π²ΡΠ΅ΠΌ ΡΡΠ΅Π±ΠΎΠ²Π°Π½ΠΈΡΠΌ Π°Π»ΡΠΌΠΈΠ½ΠΈΠ΅Π²ΠΎΠΉ
ΠΏΡΠΎΠΌΡΡΠ»Π΅Π½Π½ΠΎΡΡΠΈ. Π ΡΡΠ°ΡΡΠ΅ Ρ ΡΠΎΡΠΊΠΈ Π·ΡΠ΅Π½ΠΈΡ ΠΌΠΈΡΠΎΠ²ΠΎΠ³ΠΎ ΠΎΠΏΡΡΠ° Π°Π»ΡΠΌΠΈΠ½ΠΈΠ΅Π²ΠΎΠΉ ΠΏΡΠΎΠΌΡΡΠ»Π΅Π½Π½ΠΎΡΡΠΈ
ΡΠ°ΡΡΠΌΠΎΡΡΠ΅Π½Ρ Π²ΠΎΠΏΡΠΎΡΡ ΡΠΎΡΠΌΠΈΡΠΎΠ²Π°Π½ΠΈΡ ΡΠ²ΠΎΠΉΡΡΠ² ΠΊΠΎΠΊΡΠ° ΠΎΡ Π½Π°ΡΠ°Π»Π° Π½Π΅ΡΡΠ΅ΠΏΠ΅ΡΠ΅ΡΠ°Π±ΠΎΡΠΊΠΈ Π΄ΠΎ ΡΠΊΠ»Π°Π΄Π°
ΡΡΡΡΡ Π°Π½ΠΎΠ΄Π½ΠΎΠ³ΠΎ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π°. ΠΡΠ΅Π΄Π»Π°Π³Π°Π΅ΠΌΠ°Ρ ΡΡΠ°ΡΡΡ ΡΠ²Π»ΡΠ΅ΡΡΡ ΠΏΠ΅ΡΠ²ΠΎΠΉ Π² ΡΠ΅ΡΠΈΠΈ ΡΠΎΠ²ΠΌΠ΅ΡΡΠ½ΡΡ
ΡΠ°Π±ΠΎΡ ΡΠΎΡΡΡΠ΄Π½ΠΈΠΊΠΎΠ² Π‘ΠΈΠ±ΠΈΡΡΠΊΠΎΠ³ΠΎ ΡΠ΅Π΄Π΅ΡΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΡΠ½ΠΈΠ²Π΅ΡΡΠΈΡΠ΅ΡΠ° ΠΈ ΡΠΏΠ΅ΡΠΈΠ°Π»ΠΈΡΡΠΎΠ² ΠΡΠΈΠ½ΡΠΊΠΎΠ³ΠΎ ΠΠΠ,
ΠΏΠΎΡΠ²ΡΡΠ΅Π½Π½ΡΡ
ΡΡΡΠΎΠΈΡΠ΅Π»ΡΡΡΠ²Ρ ΠΈ ΡΠ°Π·Π²ΠΈΡΠΈΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΡΡΠ²Π° Π½Π΅ΡΡΡΠ½ΠΎΠ³ΠΎ ΠΊΠΎΠΊΡΠ° Π½Π° ΠΡΠΈΠ½ΡΠΊΠΎΠΌ ΠΠΠ.Petroleum coke is the main raw material for aluminum electrolysis anodes. Quality of coke determinates
the technology, ecology and economics of production of aluminum. From the aluminum producers
point of view, petroleum coke should have the following characteristics:
- a minimum ash content and the absence of impurities,
- high resistance to oxygen and CO2,
- low porosity and electrical resistivity
- mechanical strength, acceptable for processing
- good microstructure.
Petroleum coke is produced from petroleum residues and secondary petroleum products. Because of
the peculiarity of the technology, the quality of petroleum coke is a compromise between the receipt of
light fuel and raw coking. It is not surprising that only a very small amount of coke can satisfy all the
requirements of the aluminum industry. The purpose this article is formation of cokes properties from
the beginning of oil refining up to the anode plant. The article is the first in a lot of cooperated works
of the Siberian Federal University and specialists of the Achinsk refinery, dedicated to construction
and development of production of petroleum coke at the Achinsk refinery
Complex Research of Liquid Products of Delayed Coking of Heavy Petroleum Residues of βAchinsk Refineryβ
ΠΡΡΡΠ΅ΡΡΠ²Π»Π΅Π½ΠΎ ΠΊΠΎΠΌΠΏΠ»Π΅ΠΊΡΠ½ΠΎΠ΅ ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΠ΅ ΠΈΠ½Π΄ΠΈΠ²ΠΈΠ΄ΡΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΠΈ Π³ΡΡΠΏΠΏΠΎΠ²ΠΎΠ³ΠΎ ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΠ½ΠΎΠ³ΠΎ
ΡΠΎΡΡΠ°Π²Π°, ΡΠΈΠ·ΠΈΠΊΠΎ-Ρ
ΠΈΠΌΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»Π΅ΠΉ ΠΆΠΈΠ΄ΠΊΠΈΡ
ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ², ΠΎΠ±ΡΠ°Π·ΡΡΡΠΈΡ
ΡΡ ΠΏΡΠΈ ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΠΈ
Π³ΡΠ΄ΡΠΎΠ½Π° ΠΠΠ Β«ΠΠΠΠ ΠΠΠΒ» ΠΏΡΠΈ ΡΠ°Π·Π»ΠΈΡΠ½ΡΡ
ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ°Ρ
ΠΈ Π΄Π°Π²Π»Π΅Π½ΠΈΠΈ ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΡ, Π΄Π»Ρ ΠΎΡΠ΅Π½ΠΊΠΈ
Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΠΈ ΠΈΡ
Π²ΠΎΠ²Π»Π΅ΡΠ΅Π½ΠΈΡ Π² Π½ΠΎΠΌΠ΅Π½ΠΊΠ»Π°ΡΡΡΡ ΡΠΎΠ²Π°ΡΠ½ΠΎΠΉ ΠΏΡΠΎΠ΄ΡΠΊΡΠΈΠΈ. ΠΡΠΎΠ±ΠΎΠ΅ Π²Π½ΠΈΠΌΠ°Π½ΠΈΠ΅ ΡΠ΄Π΅Π»Π΅Π½ΠΎ
ΠΊΠΎΠ»ΠΈΡΠ΅ΡΡΠ²Π΅Π½Π½ΡΠΌ ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»ΡΠΌ ΡΠ³Π»Π΅Π²ΠΎΠ΄ΠΎΡΠΎΠ΄Π½ΠΎΠ³ΠΎ ΡΠΎΡΡΠ°Π²Π° Π΄ΠΈΡΡΠΈΠ»Π»ΡΡΠ½ΠΎΠΉ ΡΡΠ°ΠΊΡΠΈΠΈ, Π° ΡΠ°ΠΊΠΆΠ΅
ΠΎΡΠ΅Π½ΠΊΠ΅ ΡΠΎΠ΄Π΅ΡΠΆΠ°Π½ΠΈΡ ΠΎΠ±ΡΠ΅ΠΉ ΠΈ ΠΌΠ΅ΡΠΊΠ°ΠΏΡΠ°Π½ΠΎΠ²ΠΎΠΉ ΡΠ΅ΡΡ. ΠΡΡΠ²Π»Π΅Π½Ρ Π·Π°ΠΊΠΎΠ½ΠΎΠΌΠ΅ΡΠ½ΠΎΡΡΠΈ ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΠΉ
ΡΠΎΡΡΠ°Π²Π° ΠΈ ΡΠ²ΠΎΠΉΡΡΠ² ΡΠ·ΠΊΠΈΡ
ΡΡΠ°ΠΊΡΠΈΠΉ ΠΆΠΈΠ΄ΠΊΠΈΡ
ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ² ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΡ ΠΎΡ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΠΎΠ² ΠΏΡΠΎΡΠ΅ΡΡΠ°. Π Π°Π·ΡΠ°Π±ΠΎΡΠ°Π½Ρ ΠΏΡΠ΅Π΄Π²Π°ΡΠΈΡΠ΅Π»ΡΠ½ΡΠ΅ ΡΠ΅ΠΊΠΎΠΌΠ΅Π½Π΄Π°ΡΠΈΠΈ ΠΏΠΎ Π΄ΠΎΡΡΠΈΠΆΠ΅Π½ΠΈΡ
ΠΌΠ°ΠΊΡΠΈΠΌΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»Ρ Π²ΡΡ
ΠΎΠ΄Π° ΠΈ ΠΎΠΏΡΠΈΠΌΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΡΠ³Π»Π΅Π²ΠΎΠ΄ΠΎΡΠΎΠ΄Π½ΠΎΠ³ΠΎ ΡΠΎΡΡΠ°Π²Π° Π΄ΠΈΡΡΠΈΠ»Π»ΡΡΠ½ΡΡ
ΡΡΠ°ΠΊΡΠΈΠΉCarried out a comprehensive study of individual and group component composition, physical and
chemical parameters of liquid products formed during coking tar of Β«Achinsk RefineryΒ» at various
temperatures and pressures coking in order to assess the possibility of involving them in the range
of marketable products. Special attention is paid to the quantitative indicators of the hydrocarbon
composition of distillate fraction, as well as evaluating the content of general and mercaptan sulfur.
Revealed regularities of changes in the composition and properties of narrow fractions of liquid products
of coking on the technological parameters of the process. Developed preliminary recommendations
for the achievement of the maximum rate of output and optimal hydrocarbon composition of distillate
fraction
Complex Research of Liquid Products of Delayed Coking of Heavy Petroleum Residues of βAchinsk Refineryβ
ΠΡΡΡΠ΅ΡΡΠ²Π»Π΅Π½ΠΎ ΠΊΠΎΠΌΠΏΠ»Π΅ΠΊΡΠ½ΠΎΠ΅ ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΠ΅ ΠΈΠ½Π΄ΠΈΠ²ΠΈΠ΄ΡΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΠΈ Π³ΡΡΠΏΠΏΠΎΠ²ΠΎΠ³ΠΎ ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΠ½ΠΎΠ³ΠΎ
ΡΠΎΡΡΠ°Π²Π°, ΡΠΈΠ·ΠΈΠΊΠΎ-Ρ
ΠΈΠΌΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»Π΅ΠΉ ΠΆΠΈΠ΄ΠΊΠΈΡ
ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ², ΠΎΠ±ΡΠ°Π·ΡΡΡΠΈΡ
ΡΡ ΠΏΡΠΈ ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΠΈ
Π³ΡΠ΄ΡΠΎΠ½Π° ΠΠΠ Β«ΠΠΠΠ ΠΠΠΒ» ΠΏΡΠΈ ΡΠ°Π·Π»ΠΈΡΠ½ΡΡ
ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ°Ρ
ΠΈ Π΄Π°Π²Π»Π΅Π½ΠΈΠΈ ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΡ, Π΄Π»Ρ ΠΎΡΠ΅Π½ΠΊΠΈ
Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΠΈ ΠΈΡ
Π²ΠΎΠ²Π»Π΅ΡΠ΅Π½ΠΈΡ Π² Π½ΠΎΠΌΠ΅Π½ΠΊΠ»Π°ΡΡΡΡ ΡΠΎΠ²Π°ΡΠ½ΠΎΠΉ ΠΏΡΠΎΠ΄ΡΠΊΡΠΈΠΈ. ΠΡΠΎΠ±ΠΎΠ΅ Π²Π½ΠΈΠΌΠ°Π½ΠΈΠ΅ ΡΠ΄Π΅Π»Π΅Π½ΠΎ
ΠΊΠΎΠ»ΠΈΡΠ΅ΡΡΠ²Π΅Π½Π½ΡΠΌ ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»ΡΠΌ ΡΠ³Π»Π΅Π²ΠΎΠ΄ΠΎΡΠΎΠ΄Π½ΠΎΠ³ΠΎ ΡΠΎΡΡΠ°Π²Π° Π΄ΠΈΡΡΠΈΠ»Π»ΡΡΠ½ΠΎΠΉ ΡΡΠ°ΠΊΡΠΈΠΈ, Π° ΡΠ°ΠΊΠΆΠ΅
ΠΎΡΠ΅Π½ΠΊΠ΅ ΡΠΎΠ΄Π΅ΡΠΆΠ°Π½ΠΈΡ ΠΎΠ±ΡΠ΅ΠΉ ΠΈ ΠΌΠ΅ΡΠΊΠ°ΠΏΡΠ°Π½ΠΎΠ²ΠΎΠΉ ΡΠ΅ΡΡ. ΠΡΡΠ²Π»Π΅Π½Ρ Π·Π°ΠΊΠΎΠ½ΠΎΠΌΠ΅ΡΠ½ΠΎΡΡΠΈ ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΠΉ
ΡΠΎΡΡΠ°Π²Π° ΠΈ ΡΠ²ΠΎΠΉΡΡΠ² ΡΠ·ΠΊΠΈΡ
ΡΡΠ°ΠΊΡΠΈΠΉ ΠΆΠΈΠ΄ΠΊΠΈΡ
ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ² ΠΊΠΎΠΊΡΠΎΠ²Π°Π½ΠΈΡ ΠΎΡ ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΠΎΠ² ΠΏΡΠΎΡΠ΅ΡΡΠ°. Π Π°Π·ΡΠ°Π±ΠΎΡΠ°Π½Ρ ΠΏΡΠ΅Π΄Π²Π°ΡΠΈΡΠ΅Π»ΡΠ½ΡΠ΅ ΡΠ΅ΠΊΠΎΠΌΠ΅Π½Π΄Π°ΡΠΈΠΈ ΠΏΠΎ Π΄ΠΎΡΡΠΈΠΆΠ΅Π½ΠΈΡ
ΠΌΠ°ΠΊΡΠΈΠΌΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΠΏΠΎΠΊΠ°Π·Π°ΡΠ΅Π»Ρ Π²ΡΡ
ΠΎΠ΄Π° ΠΈ ΠΎΠΏΡΠΈΠΌΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΡΠ³Π»Π΅Π²ΠΎΠ΄ΠΎΡΠΎΠ΄Π½ΠΎΠ³ΠΎ ΡΠΎΡΡΠ°Π²Π° Π΄ΠΈΡΡΠΈΠ»Π»ΡΡΠ½ΡΡ
ΡΡΠ°ΠΊΡΠΈΠΉCarried out a comprehensive study of individual and group component composition, physical and
chemical parameters of liquid products formed during coking tar of Β«Achinsk RefineryΒ» at various
temperatures and pressures coking in order to assess the possibility of involving them in the range
of marketable products. Special attention is paid to the quantitative indicators of the hydrocarbon
composition of distillate fraction, as well as evaluating the content of general and mercaptan sulfur.
Revealed regularities of changes in the composition and properties of narrow fractions of liquid products
of coking on the technological parameters of the process. Developed preliminary recommendations
for the achievement of the maximum rate of output and optimal hydrocarbon composition of distillate
fraction