1. OILS OF DISTILLATION OF COAL TAR: - ABSORBING OIL / ACEITE PESADO-WASH OIL: 24 70 TN. REPRESENTS OPAQUE MOBILE LIQUID OF DARK BROWN COLOR THE MIXED PRODUCT IN WHICH AROMATIC COMPONENTS PREVAIL AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (1 1 BIPHENYL 2-METHYL-1 1-BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METHYLNAPHTHALENE FLUORENE ACENAPHTHYLENE AND OTHER NAPHTHALENE DERIVATIVES PHENANTHRENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE ISOQUINOLINE INDOLE QUINALDIN OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZO [B] THIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN 4-METHYLDIBENZOFURAN). IS 1050 +/- 1 KG / M3. AT A TEMPERATURE OF 250 DEGREES CELSIUS. DISTILLED: 38.0 +/- 0.5 VOL.% FRACTIONAL COMPOSITION: BOILING POINT: 232 +/- 0.5 DEG.C.THE BOILING POINT TEMPERATURE: 285.8 +/- 0.5 DEG.C.5OB .% DISTILLED AT A TEMPERATURE OF: 239.5 +/- 0.5 DEG.C.95OB.% DISTILLED AT A TEMPERATURE OF: 274.4 +/- 0.5 DEG.C.PERCENTAGE: 99.5 +/- 0.5 VOL.% RESIDUE AFTER DISTILLATION: 0.5 +/- 0.1 VOL.% USED IN THE TECHNOLOGICAL PROCESS OF THE CAPTURE PLANT OF COKE PRODUCTION IN THE PRODUCTION OF CRUDE BENZENE FOR THE EXTRACTION OF BENZENE HYDROCARBONS FROM COKE OVEN GAS FOLLOWED BY DISTILLATION IN DISTILLATION COLUMNS.
1. OILS OF DISTILLATION OF COAL TAR: - ABSORBING OIL / ACEITE PESADO-WASH OIL: 24 70 TN. REPRESENTS OPAQUE MOBILE LIQUID OF DARK BROWN COLOR THE MIXED PRODUCT IN WHICH AROMATIC COMPONENTS PREVAIL AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (1 1 BIPHENYL 2-METHYL-1 1-BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METHYLNAPHTHALENE FLUORENE ACENAPHTHYLENE AND OTHER NAPHTHALENE DERIVATIVES PHENANTHRENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE ISOQUINOLINE INDOLE QUINALDIN OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZO [B] THIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN 4-METHYLDIBENZOFURAN). IS 1050 +/- 1 KG / M3. AT A TEMPERATURE OF 250 DEGREES CELSIUS. DISTILLED: 38.0 +/- 0.5 VOL.% FRACTIONAL COMPOSITION: BOILING POINT: 232 +/- 0.5 DEG.C.THE BOILING POINT TEMPERATURE: 285.8 +/- 0.5 DEG.C.5OB .% DISTILLED AT A TEMPERATURE OF: 239.5 +/- 0.5 DEG.C.95OB.% DISTILLED AT A TEMPERATURE OF: 274.4 +/- 0.5 DEG.C.PERCENTAGE: 99.5 +/- 0.5 VOL.% RESIDUE AFTER DISTILLATION: 0.5 +/- 0.1 VOL.% USED IN THE TECHNOLOGICAL PROCESS OF THE CAPTURE PLANT OF COKE PRODUCTION IN THE PRODUCTION OF CRUDE BENZENE FOR THE EXTRACTION OF BENZENE HYDROCARBONS FROM COKE OVEN GAS FOLLOWED BY DISTILLATION IN DISTILLATION COLUMNS.
1. OILS OF DISTILLATION OF COAL TAR: - ABSORBENT OIL / ACEITE PESADO-WASH OIL: 23 12 TN. REPRESENTS OPAQUE MOBILE LIQUID OF DARK BROWN COLOR THE MIXED PRODUCT IN WHICH AROMATIC COMPONENTS PREVAIL AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METHYLNAPHTHALENE FLUORENE ACENAPHTHALENE AND OTHER NAPHTHALENE DERIVATIVES) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE QUINOQUINOLINE OTHER) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (3-METHYL-1-BENZOTHIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN). DENSITY AT 25 DEG.C. MAKES 1055 +/- 1 KG / M3. FRACTIONAL STRUCTURE: TEMPERATURE OF THE BEGINNING OF BOILING: 248 +/- 0 5 DEG.TS.TEMPERATURE OF THE END OF BOILING: 286 +/- 0 5 DEG.TS.5OB.% IS DISTILLED AT A TEMPERATURE: 250 +/- 0.5 DEG.C.95OB.% IS DISTILLED AT A TEMPERATURE OF: 274 +/- 0.5 DEG.C.AT 250 DEG.C. DISTILLED: 5.0 +/- 0.5 VOL.% PERCENTAGE OF DISTILLATION: 99.0 +/- 0.5 VOL.% RESIDUE AFTER DISTILLATION: 1.0 +/- 0
1. OILS OF DISTILLATION OF COAL TAR: - ABSORBENT OIL / ACEITE PESADO-WASH OIL: 23 12 TN. REPRESENTS OPAQUE MOBILE LIQUID OF DARK BROWN COLOR THE MIXED PRODUCT IN WHICH AROMATIC COMPONENTS PREVAIL AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METHYLNAPHTHALENE FLUORENE ACENAPHTHALENE AND OTHER NAPHTHALENE DERIVATIVES) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE QUINOQUINOLINE OTHER) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (3-METHYL-1-BENZOTHIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN). DENSITY AT 25 DEG.C. MAKES 1055 +/- 1 KG / M3. FRACTIONAL STRUCTURE: TEMPERATURE OF THE BEGINNING OF BOILING: 248 +/- 0 5 DEG.TS.TEMPERATURE OF THE END OF BOILING: 286 +/- 0 5 DEG.TS.5OB.% IS DISTILLED AT A TEMPERATURE: 250 +/- 0.5 DEG.C.95OB.% IS DISTILLED AT A TEMPERATURE OF: 274 +/- 0.5 DEG.C.AT 250 DEG.C. DISTILLED: 5.0 +/- 0.5 VOL.% PERCENTAGE OF DISTILLATION: 99.0 +/- 0.5 VOL.% RESIDUE AFTER DISTILLATION: 1.0 +/- 0
07-June-2021
2707991900
1.MASLO COAL ABSORBING -59250KH LOT NUMBER 7140 MARCO UNDER THE AGREEMENT 60009YAVLYAYE ORDER ITSELF TRANSPARENT MOBILE LIQUID OF DARK BROWN COLOR WITH SPECIFICODOR (PHENOLIC) MIXED PRODUCT IN WHICH DOMINATES AROMATIC COMPONENTS AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (1 1-BIPHENYL 2-METHYL-1 1-BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METYLNAFTALIN FLOUREN ATSENAFTILEN AND OTHER DERIVATIVES OF NAPHTHALENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUND (QUINOLINE ISOQUINOLINE INDOLE OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZO (B) THIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN 4 METYLDIBENZOFURAN) 3-METYLFENOL. FRACTIONAL COMPOSITION: -TEMPERATURE OF BOILING ° C - 218 +/- 0 5; -5OB % DISTURBED AT TEMPERATURE DEG.C -229 1 +/- 0 5; -95OB % DISTILLED AT TEMPERATURE GRAD.C -279 6 +/- 0 5; -TEMPERATURE OF THE END OF BOILING DEG.C -284 5 +/- 0 5; -250 DEG.C DISTILLED ABOUT % -51 0 +/- 0 5; 98.0 +/- 0.5; -REST AFTER DISTILLATION VOL % -2.0 +/- 0.5; -LOSS DURING DISTILLATION ABOUT % -0; SAMPLE DENSITY AT 15 DEG.C IS (1059 +/- 1) KG / M3; AT A TEMPERATURE OF 250 DEG.C IS DISTILLED (51.0 +/- 0.5) BY VOLUME;; TAR OIL IS ACID-BASE OCHYSTKOYUPOHLYNALNOYI FRACTION AND ARE USED MAINLY FOR ABSORBTSIYIZ COKE OVEN GAS BENZENE AND ITS HOMOLOGUES AND OTHER PREPARATION MASEL.FIZYCHNO AND CHEMICAL PROPERTIES: -OB'YEMNA FATE OF WATER -0.3%; -MASOVA NAPHTHALENE SHARE% -25.7; -MASS SHARE OF PHENOLS % -3 0; -FRACTIONAL COMPOSITION %: 230 -20 230-300 -78; -DENSITY AT 20 DEG.C KG / M3 -1054; TU 2457-170 -00190437-2002 ??.1
1.MASLO COAL ABSORBING -59250KH LOT NUMBER 7140 MARCO UNDER THE AGREEMENT 60009YAVLYAYE ORDER ITSELF TRANSPARENT MOBILE LIQUID OF DARK BROWN COLOR WITH SPECIFICODOR (PHENOLIC) MIXED PRODUCT IN WHICH DOMINATES AROMATIC COMPONENTS AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (1 1-BIPHENYL 2-METHYL-1 1-BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METYLNAFTALIN FLOUREN ATSENAFTILEN AND OTHER DERIVATIVES OF NAPHTHALENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUND (QUINOLINE ISOQUINOLINE INDOLE OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZO (B) THIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN 4 METYLDIBENZOFURAN) 3-METYLFENOL. FRACTIONAL COMPOSITION: -TEMPERATURE OF BOILING ° C - 218 +/- 0 5; -5OB % DISTURBED AT TEMPERATURE DEG.C -229 1 +/- 0 5; -95OB % DISTILLED AT TEMPERATURE GRAD.C -279 6 +/- 0 5; -TEMPERATURE OF THE END OF BOILING DEG.C -284 5 +/- 0 5; -250 DEG.C DISTILLED ABOUT % -51 0 +/- 0 5; 98.0 +/- 0.5; -REST AFTER DISTILLATION VOL % -2.0 +/- 0.5; -LOSS DURING DISTILLATION ABOUT % -0; SAMPLE DENSITY AT 15 DEG.C IS (1059 +/- 1) KG / M3; AT A TEMPERATURE OF 250 DEG.C IS DISTILLED (51.0 +/- 0.5) BY VOLUME;; TAR OIL IS ACID-BASE OCHYSTKOYUPOHLYNALNOYI FRACTION AND ARE USED MAINLY FOR ABSORBTSIYIZ COKE OVEN GAS BENZENE AND ITS HOMOLOGUES AND OTHER PREPARATION MASEL.FIZYCHNO AND CHEMICAL PROPERTIES: -OB'YEMNA FATE OF WATER -0.3%; -MASOVA NAPHTHALENE SHARE% -25.7; -MASS SHARE OF PHENOLS % -3 0; -FRACTIONAL COMPOSITION %: 230 -20 230-300 -78; -DENSITY AT 20 DEG.C KG / M3 -1054; TU 2457-170 -00190437-2002 ??.1
07-October-2020
2707991900
1.MASLO COAL ABSORBING -257250KH.DATA MANUFACTURING 15.09.2020R 16.09.2020R.YAVLYAYE ITSELF TRANSPARENT MOBILE LIQUID OF DARK BROWN COLOR MIXED PRODUCT IN WHICH DOMINATES AROMATIC COMPONENTS AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METYLNAFTALIN FLOUREN ATSENAFTALIN AND OTHER DERIVATIVES OF NAPHTHALENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE ISOQUINOLINE INDOLE HINALDIN OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZOTIOFEN) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN) .MASLO COAL POWER IN THE PROCESS OF RECTIFICATION (DISTILLATION HIGH) PITCH COAL AND DESIGNED TO CAPTURE THE BENZENE CARBOHYDRATE PREPARATION OF TECHNICAL OILS AND ADDITIVES PHYSICAL AND CHEMICAL PROPERTIES: -VMIST WATER % -0.4; -FRACTIONAL COMPOSITION UP TO 230 DEG.C % - ABSENT; -FRACTIONAL COMPOSITION 230-300GRAD.C % -91; -MASS SHARE OF NAPHTHALINE % -21.4; -MASS SHARE - PHENOL 1.6
1.MASLO COAL ABSORBING -257250KH.DATA MANUFACTURING 15.09.2020R 16.09.2020R.YAVLYAYE ITSELF TRANSPARENT MOBILE LIQUID OF DARK BROWN COLOR MIXED PRODUCT IN WHICH DOMINATES AROMATIC COMPONENTS AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METYLNAFTALIN FLOUREN ATSENAFTALIN AND OTHER DERIVATIVES OF NAPHTHALENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE ISOQUINOLINE INDOLE HINALDIN OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZOTIOFEN) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN) .MASLO COAL POWER IN THE PROCESS OF RECTIFICATION (DISTILLATION HIGH) PITCH COAL AND DESIGNED TO CAPTURE THE BENZENE CARBOHYDRATE PREPARATION OF TECHNICAL OILS AND ADDITIVES PHYSICAL AND CHEMICAL PROPERTIES: -VMIST WATER % -0.4; -FRACTIONAL COMPOSITION UP TO 230 DEG.C % - ABSENT; -FRACTIONAL COMPOSITION 230-300GRAD.C % -91; -MASS SHARE OF NAPHTHALINE % -21.4; -MASS SHARE - PHENOL 1.6
04-October-2021
2707991900
1.MASLO COAL ABSORBING -61300KH LOT NUMBER 10083 MARCHE UNDER THE AGREEMENT 60009YAVLYAYE ORDER ITSELF TRANSPARENT MOBILE LIQUID OF DARK BROWN COLOR WITH SPECIFICODOR (PHENOLIC) MIXED PRODUCT IN WHICH DOMINATES AROMATIC COMPONENTS AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (1 1-BIPHENYL 2-METHYL-1 1-BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METYLNAFTALIN FLOUREN ATSENAFTILEN AND OTHER DERIVATIVES OF NAPHTHALENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE ISOQUINOLINE INDOLE OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZO (B) THIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN 4 METYLDIBENZOFURAN) 3-METYLFENOL. FRACTIONAL COMPOSITION: -TEMPERATURE OF THE BEGINNING OF BOILING DEG.C -218 +/- 0 5; -5OB % DISTURBED AT TEMPERATURE DEG.C -229 1 +/- 0 5; -95OB % PEREGAN DEG.C -279.6 +/- 0.5; -TEMPERATURE OF THE END OF BOILING DEG.C -284.5 +/- 0.5; -250 DEG.C DISTANCE ABOUT % -51.0 +/- 0 5; -PERCENTAGE OF DISTILLATION ABOUT % -98 0 +/- 0 5; -BALANCES AFTER DISTILLATION ABOUT % -2 0 +/- 0 5; -LOSS IN DISTILLMENT ABOUT % -0; SAMPLE DENSITY AT 15 DEG.C IS (1059 +/- 1) KG / M3; AT A TEMPERATURE OF 250 DEG.C IS DISTILLED (51.0 +/- 0.5) BY VOLUME;%; TAR OIL IS ACID-BASE OCHYSTKOYUPOHLYNALNOYI FRACTION AND ARE USED MAINLY FOR ABSORBTSIYIZ COKE OVEN GAS BENZENE AND ITS HOMOLOGUES AND OTHER PREPARATION MASEL.FIZYCHNO AND CHEMICAL PROPERTIES: -OB'YEMNA FATE OF WATER -0.1%; -MASOVA NAPHTHALENE SHARE% -23.5; -MASS CONTENT OF PHENOLS % -2.9; -FRACTIONAL COMPOSITION %: 230 -18; 230-300 -80; -DENSITY AT 20 DEG.C KG / M3 -1058; TU 2457-170-00190437-2002 MR.1
1.MASLO COAL ABSORBING -61300KH LOT NUMBER 10083 MARCHE UNDER THE AGREEMENT 60009YAVLYAYE ORDER ITSELF TRANSPARENT MOBILE LIQUID OF DARK BROWN COLOR WITH SPECIFICODOR (PHENOLIC) MIXED PRODUCT IN WHICH DOMINATES AROMATIC COMPONENTS AND WHICH CONTAINS INCLUDING: AROMATIC HYDROCARBONS (1 1-BIPHENYL 2-METHYL-1 1-BIPHENYL 4-METHYL-1 1-BIPHENYL) CONDENSED AROMATIC COMPOUNDS (NAPHTHALENE 1-METYLNAFTALIN FLOUREN ATSENAFTILEN AND OTHER DERIVATIVES OF NAPHTHALENE) AROMATIC NITROGEN-CONTAINING HETEROCYCLIC COMPOUNDS (QUINOLINE ISOQUINOLINE INDOLE OTHER DERIVATIVES) SULFUR-CONTAINING HETEROCYCLIC COMPOUNDS (BENZO (B) THIOPHENE) OXYGEN-CONTAINING HETEROCYCLIC COMPOUNDS (DIBENZOFURAN 4 METYLDIBENZOFURAN) 3-METYLFENOL. FRACTIONAL COMPOSITION: -TEMPERATURE OF THE BEGINNING OF BOILING DEG.C -218 +/- 0 5; -5OB % DISTURBED AT TEMPERATURE DEG.C -229 1 +/- 0 5; -95OB % PEREGAN DEG.C -279.6 +/- 0.5; -TEMPERATURE OF THE END OF BOILING DEG.C -284.5 +/- 0.5; -250 DEG.C DISTANCE ABOUT % -51.0 +/- 0 5; -PERCENTAGE OF DISTILLATION ABOUT % -98 0 +/- 0 5; -BALANCES AFTER DISTILLATION ABOUT % -2 0 +/- 0 5; -LOSS IN DISTILLMENT ABOUT % -0; SAMPLE DENSITY AT 15 DEG.C IS (1059 +/- 1) KG / M3; AT A TEMPERATURE OF 250 DEG.C IS DISTILLED (51.0 +/- 0.5) BY VOLUME;%; TAR OIL IS ACID-BASE OCHYSTKOYUPOHLYNALNOYI FRACTION AND ARE USED MAINLY FOR ABSORBTSIYIZ COKE OVEN GAS BENZENE AND ITS HOMOLOGUES AND OTHER PREPARATION MASEL.FIZYCHNO AND CHEMICAL PROPERTIES: -OB'YEMNA FATE OF WATER -0.1%; -MASOVA NAPHTHALENE SHARE% -23.5; -MASS CONTENT OF PHENOLS % -2.9; -FRACTIONAL COMPOSITION %: 230 -18; 230-300 -80; -DENSITY AT 20 DEG.C KG / M3 -1058; TU 2457-170-00190437-2002 MR.1