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Apparatus for the removal of volatile and gaseous components occluded in oils

机译:用于去除油中所含的挥发性和气态成分的设备

摘要

Volatile impurities and water are removed from contaminated heavy oils, such as oils separated from oily-water on board ship, by heating the contaminated oil in a settlement chamber, whereby residual water separates out from the oil, and causing the hot oil to flow by gravity in four thin streams down inclined trays 88, 89, 90 and plate 13 (Figs. 1 and 2) or to cascade as a single thin stream down inclined trays 187, 188, 189, 190 (Fig. 8), the apparatus being maintained at a sub-atmospheric pressure, e.g. by a vacuum pump (not shown) attached to a steam-injection extractor at the top of the apparatus. In the apparatus shown in Figs. 1 and 2, the oil is heated in the lower chamber 12 by steam-pipes 30, and the hot oil then rises to the manifold 97 which supplies the upper ends of the trays and the plate 13. In Fig. 8, the trays themselves are heated, by steam-jackets 192; and the oil-to-be-treated is supplied to the top tray via inlet 181. The vessel shown in Figs. 1 and 2 is divided into two chambers 11 and 12 by the plate 13; and the upper chamber is divided by side-plates 14 into a central chamber and two side settlement tanks 15, 16. The latter communicate with the lower chamber 12 via holes 58 and slots 59 (Fig. 4). The oil-to-be-treated is pumped via pipe 27 into chamber 12, where it is heated to about 200 DEG F. The hot oil rises up through holes 58 into tanks 15 and 16, from which it flows via pipes 63, 64, 65 and valve 60 to manifold 97. The oil then flows down pipes 99 which supplies it to the three trays and the plate 13 via orifices 103, 104, 105 and 102. Plates 106 and 107 ensure an even distribution of oil as it flows down the trays and the plate 13. The oil flows off the trays through funnel-tubes 96, and is collected in two chambers. The oil flowing off plate 13 is collected in the same chambers. The treated oil is removed from the apparatus via float-valve 112. Water, which has separated from the oil in chamber 12 and tanks 15, 16, collects in the bottom of chamber 12, and is withdrawn via valve 142. Thick deposits on steam-pipes 30 are dislodged by moving scraper-plates 41 longitudinally along the pipes by means of handle 55, threaded rod 47 and threaded bush 46. In Fig. 8, the jackets 192 are connected in series; and steam is passed through them from the lowest tray to the highest, the steamsupply to the lowest being taken from coil 205 in the oil-receiving space in the lower part of the vessel. The oil running off the lowest tray is collected in chamber 200, and finally withdrawn from the vessel through outlet 204. Air may be introduced into the vessel through perforated ring 206 in order to assist the separation of volatile constituents from the oil. PICT:0974857/C4-C5/1 PICT:0974857/C4-C5/2 PICT:0974857/C4-C5/3 PICT:0974857/C4-C5/4
机译:通过在沉降室中加热受污染的油,从受污染的重油(例如从船上从含油水中分离出的油)中除去挥发性杂质和水,从而使残留的水从油中分离出来,并使热油流过在向下倾斜的塔板88、89、90和板13(图1和2)的四个细流中产生重力,或作为单个向下倾斜的塔板187、188、189、190的稀流级联(图8),该设备是保持低于大气压,例如通过连接到装置顶部的蒸汽注入提取器上的真空泵(未显示)进行。在图1和图2所示的装置中。如图1和图2所示,油在下部腔室12中被蒸汽管30加热,然后热油上升到歧管97,歧管97为塔盘和板13的上端供料。在图8中,塔盘本身通过蒸汽夹套192加热;然后,通过入口181将被处理油供给至上塔板。图1和2由板13分成两个腔室11和12。上部腔室由侧板14划分为中央腔室和两个侧向沉降槽15、16。侧向沉降槽15、16通过孔58和狭槽59与下部腔室12连通(图4)。待处理的油通过管道27泵入腔室12,在其中加热到约200°F。热油通过孔58上升到油箱15和16中,并通过管道63、64从中流动。 ,65和阀60到达歧管97。然后,油向下流经管道99,通过孔103、104、105和102将其供应到三个塔板和板13。板106和107确保油在流动时均匀分布向下流过塔板和板13。油通过漏斗管96从塔板流出,并收集在两个腔室中。从板13流出的油被收集在相同的腔室中。经处理的油通过浮子阀112从设备中除去。与腔室12和油箱15、16中的油分离的水聚集在腔室12的底部,并通过阀142抽出。蒸汽上有厚的沉积物通过用手柄55,螺纹杆47和螺纹衬套46使刮板41沿管子纵向移动,使管子30移开。在图8中,外套192串联连接;管套192串联连接。蒸汽从最低的塔板流到最高的塔板,而蒸汽的最低供应则从容器下部的油接收空间中的盘管205取走。从最低塔盘流出的油收集在腔室200中,最后通过出口204从容器中抽出。可以通过穿孔环206将空气引入容器,以帮助从油中分离出挥发性成分。

著录项

  • 公开/公告号GB974857A

    专利类型

  • 公开/公告日1964-11-11

    原文格式PDF

  • 申请/专利权人 DOUGLAS GEORGE UNTHANK;HENRY ARTHUR JOHN SILLEY;

    申请/专利号GB19590042686

  • 发明设计人

    申请日1959-12-15

  • 分类号C10G33/06;

  • 国家 GB

  • 入库时间 2022-08-23 15:35:14

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