cracking distillationとは 意味・読み方・使い方

The method comprises adding 0.01-2.0 vol.%, based on the fuel oil C whole amount, of water to a fuel oil C base material selected from the bottom oil obtained from an atmospheric distillation apparatus, the bottom oil obtained from a vacuum distillation apparatus, the residual oil obtained from a bottom oil desulfurization apparatus, the residual oil obtained from a fluid catalytic cracking, and the extracted oil.例文帳に追加

常圧蒸留装置から得られる塔底油、減圧蒸留装置から得られる塔底油、残油脱硫装置から得られる残油、流動接触分解装置から得られる残油およびエキストラクト油から選ばれるＣ重油基材に、水をＣ重油全量基準で０．０１〜２．０容量％添加する。 - 特許庁

A heavy oil as a byproduct from a process of producing olefins, preferably a heavy oil containing an aromatic fraction by 85 to 99 wt.%, a 5% distillation temperature of 120 to 230°C and a 95% distillation temperature of 550 to 700°C, is subjected to thermal cracking at 400 to 600°C and under the pressure of 0.01 to 1.00 MPa.例文帳に追加

オレフィン類を製造するプロセスから副生する重質油を、好ましくは、芳香族分が８５〜９９重量％、５％留出温度が１２０〜２３０℃、及び９５％留出温度が５５０〜７００℃である重質油を、温度４００〜６００℃、圧力０．０１〜１．００ＭＰaで熱分解する重質油の熱分解方法。 - 特許庁

The asphalt burning system is provided with a solvent deasphalting apparatus 9 to perform the solvent deasphalting treatment of a vacuum distillation residual oil containing asphalt, a fluidized catalytic cracking apparatus 8 to perform the catalytic cracking of the deasphalted oil produced by the solvent deasphalting apparatus 9 to obtain a white oil, and a combustion power generation facility 16 to use the highly blown asphalt produced by the solvent deasphalting apparatus 9 as a fuel oil.例文帳に追加

アスファルトを含む減圧残渣油を溶剤脱瀝する溶剤脱瀝装置９と、該溶剤脱瀝装置９で生ずる脱瀝油を接触分解して白油化する流動接触分解装置８と、溶剤脱瀝装置９で発生する深絞りアスファルトを燃料油として用いる燃焼発電設備部１６とを備える。 - 特許庁

This method for producing a high octane value gasoline base material is characterized by catalytically cracking a heavy hydrocarbon oil in the presence of a catalytically cracking catalyst having a rare earth metal/a crystalline aluminosilicate mass ratio of ≤0.03 and then distilling the obtained production oil to obtain a fraction having a 95% distillation temperature of 90 to 150°C.例文帳に追加

希土類金属／結晶性アルミノケイ酸塩の質量比が０．０３以下の接触分解触媒を用いて重質炭化水素油を接触分解し、得られた生成油を蒸留して９５％留出温度が９０〜１５０℃である留分を取得することを特徴とする高オクタン価ガソリン基材の製造方法。 - 特許庁

In this distillation method, raw material (a) mixed with steam from a cracking furnace after pyrolysis of naphtha is fed to a lower section of a tower 1 which has trays 10 at proper intervals, the distillate (b) from the upper section of the tower is discharged to a quenching tower, and fuel oil (c) is discharged from the bottom of the tower.例文帳に追加

タナ段１０が適当な間隔で設置された塔１下部に、分解炉からナフサ熱分解後の水蒸気混合原料ａが送り込まれ、上部からは蒸留成分ｂが送り出されてクエンチ塔に至り、塔１下部からは燃料油ｃが排出される。 - 特許庁

The method for producing the crude hydroxyalkyl(meth)acrylamide having <1% content of a norbornene derivative comprises thermally cracking the norbornene derivative in a vapor phase, condensing the formed thermally cracked gas in the vapor phase, and vaporizing the obtained condensed liquid again before distillation to remove ≥50% of cyclopentadiene in the condensed liquid.例文帳に追加

ノルボルネン誘導体を気相熱分解し、生成した気相熱分解ガスを凝縮し、得られた凝縮液を、蒸留前に再蒸発することにより該凝縮液中のシクロペンタジエンを５０％以上除去して、ノルボルネン誘導体の含有量が１％未満である、粗ヒドロキシアルキル（メタ）アクリルアミドを得る。 - 特許庁

This gasoline composition formed by mixing a fraction into the composition as a base material, wherein the fraction is obtained by hydrogenating a cracked oil which is formed when ethylene is produced by thermal cracking of naphtha, contains hydrocarbon composed of five carbon atoms in an amount of ≥50 vol%, and has a freezing point of ≤ 0°C and a 90%-distillation temperature of ≤ 100°C.例文帳に追加

ナフサを熱分解してエチレンを製造する際に生成する分解油を、水素化して得られる留分であって、炭素数５の炭化水素を５０容量％以上含み、析出点が０℃以下、かつ９０％留出温度が１００℃以下である留分を基材として配合してなるガソリン組成物である。 - 特許庁

Provided is the process for the recovery and purification of the ethylene and optionally the propylene from a stream containing the lighter and heavier components that employs an ethylene distributor column and a partially thermally coupled distributed distillation system, especially the process for the recovery and purification of the ethylene and optionally the propylene from a cooled outgoing of a steam cracking furnace by a process using an ethylene distributor column.例文帳に追加

エチレン分配蒸留塔および一部熱結合分配蒸留システムを用いる、重質成分および軽質成分を含む流から、更には特に、エチレン分配塔を用いるプロセスによる水蒸気分解炉の冷却流出物からのエチレンおよび場合によってはプロピレンを回収し精製する。 - 特許庁