JPS5873362U

JPS5873362U - solid gas separator

Info

Publication number: JPS5873362U
Application number: JP16813881U
Authority: JP
Inventors: 村上　光春; 一登小林; 槙　正俊; 蛇「あ」　良峰
Original assignee: 三菱重工業株式会社; 三菱鉱業セメント株式会社
Priority date: 1981-11-11
Filing date: 1981-11-11
Publication date: 1983-05-18

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

[Brief explanation of drawings]

第１図及び第２図は夫々従来のサイクロン圧力損失の平
面図並に縦断面図、第３図は含塵ガスに対する分離器の
分離効率とサイクロン入口ガス流速との関係を示す図表
、第４図は本考案に係る固気分離器の一実施例を示す立
面図、第５図は第４図の矢視■−■図、第６図は入口ガ
ス流速と分離効率との関係の実験結果を示す図表、第７
図は傾斜集塵函の取付角度θとサイクロン圧力損失を示
　。す圧損係数ξとの関係の実験結果を示す図表である。１１・・・・・・外筒、１２・・・・・・入口管、１３
・・・・・・内筒、１４．１５・・・・・・円錐部、１
６・・・・・・傾斜集塵面、■・・・・・・入口管の軸
線、■・・・・・・第１の仮想直線、■・・・・・・第
２の仮想直線。第３匿Ｎ　　　　　　　　　　　　　低歯１１屹度サイクＤ）
１−二二で二１イグＵンー、晶覇え、イFigures 1 and 2 are a plan view and a longitudinal cross-sectional view of conventional cyclone pressure loss, Figure 3 is a chart showing the relationship between the separation efficiency of the separator for dust-containing gas and the gas flow rate at the cyclone inlet, and Figure 4 The figure is an elevational view showing one embodiment of the solid-gas separator according to the present invention, Figure 5 is a view taken along arrows ■-■ in Figure 4, and Figure 6 is an experiment on the relationship between inlet gas flow rate and separation efficiency. Chart showing the results, Part 7
The figure shows the installation angle θ of a tilted dust collection box and the cyclone pressure loss. 2 is a chart showing experimental results of the relationship between pressure loss coefficient ξ. 11...Outer cylinder, 12...Inlet pipe, 13
...Inner cylinder, 14.15...Cone part, 1
6... Inclined dust collecting surface, ■... Axis of inlet pipe, ■... First virtual straight line, ■... Second virtual straight line. 3rd Hidden N Low tooth 11 degree cycle D)
1-22 and 21 Iguun, Akira Hae, I

Claims

[Scope of utility model registration request]

Upright or inclined cylindrical outer cylinder, with one inch on the outer circumference of the outer cylinder.
an inlet pipe tangentially connected to the outer cylinder, an inner cylinder concentrically arranged inside the outer cylinder, and a lower cone connected to the lower end of the outer cylinder and having an axis obliquely intersecting with the supination cylinder axis. and an inclined dust collecting box connected to the lower end of the conical part and having an inner diameter larger than the lower end opening of the conical part, the inclined dust collecting box is connected to the lower end of the conical part, and the inclined dust collecting box is connected to the lower end of the conical part, and the inclined dust collecting box is connected to the lower end of the conical part and has an inner diameter larger than the lower end opening of the conical part. Located on the opposite side of the inlet pipe across a first imaginary straight line parallel to the axis of the pipe and passing through the axis of the outer cylinder, and with the center of the bottom plate of the inclined dust collection box and the axis of the outer cylinder A solid-gas separator characterized in that a second imaginary straight line passing through is provided at a position where the second imaginary straight line intersects the first imaginary straight line at an intersecting angle of 45° to 135°.