[go: up one dir, main page]

TW334507B - Process for the continuous conveying of a fine-grained and/or pulverized - Google Patents

Process for the continuous conveying of a fine-grained and/or pulverized

Info

Publication number
TW334507B
TW334507B TW085112626A TW85112626A TW334507B TW 334507 B TW334507 B TW 334507B TW 085112626 A TW085112626 A TW 085112626A TW 85112626 A TW85112626 A TW 85112626A TW 334507 B TW334507 B TW 334507B
Authority
TW
Taiwan
Prior art keywords
target
unit
time
target point
partial
Prior art date
Application number
TW085112626A
Other languages
Chinese (zh)
Inventor
Ing Dr Johannes Schenk Dipl
Michael Nagl Dipl-Ing
Walter Rainer Kastner Ing
Original Assignee
Voest Alpine Ind Anlagen
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Voest Alpine Ind Anlagen filed Critical Voest Alpine Ind Anlagen
Priority to TW085112626A priority Critical patent/TW334507B/en
Application granted granted Critical
Publication of TW334507B publication Critical patent/TW334507B/en

Links

Landscapes

  • Air Transport Of Granular Materials (AREA)

Abstract

According to a process for the continuous conveying of a fine-grained and/or pulverized solid to two or several target points (A to D) by means of a conveying medium, the solid is charged into a distribution vessel (7) and from there to one target point (A to D) each by means of the conveying medium via one supply line (12) each in a desired target flow rate /unit of time. To allow simple, individual adjustment of the target flow rate/ unit of time intended for one target point (A to D) at a low design-related expenditure and a high degree of operational reliability, the target now rate I unit of time intended far one target point (A to D) each is divided into two or several partial target flow rates / unit of time, one partial flow rate/ unit of time is diverted from the distribution vessel (7) by means of the conveying medium via a separate partial supply line (11), the partial target flow rates f unit of time are reunited at the respective target point (A to D) at the latest, and, in order to adjust the target now rate / unit of time at a target point (A to D) at a specific level , the partial supply the target flow rate/unit of time at a target point (A to D) at a specific level, the partial supply lines (11) leading to this target point (A to D) are alternatively kept shut-off or open.
TW085112626A 1996-10-16 1996-10-16 Process for the continuous conveying of a fine-grained and/or pulverized TW334507B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW085112626A TW334507B (en) 1996-10-16 1996-10-16 Process for the continuous conveying of a fine-grained and/or pulverized

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW085112626A TW334507B (en) 1996-10-16 1996-10-16 Process for the continuous conveying of a fine-grained and/or pulverized

Publications (1)

Publication Number Publication Date
TW334507B true TW334507B (en) 1998-06-21

Family

ID=58262976

Family Applications (1)

Application Number Title Priority Date Filing Date
TW085112626A TW334507B (en) 1996-10-16 1996-10-16 Process for the continuous conveying of a fine-grained and/or pulverized

Country Status (1)

Country Link
TW (1) TW334507B (en)

Similar Documents

Publication Publication Date Title
ZA968685B (en) Process for conveying fine-grained solid
CA2464701A1 (en) System for distributing a pulverulent material with controlled gravimetric flow rates
TW344788B (en) Continuous high pressure solids pump system
EP0698412A3 (en) Continuous starch slurry manufacture
DE59804184D1 (en) Distribution device for a circuit of a heating or cooling supply system operated with a liquid medium
AU557141B2 (en) Controlling the feed of pulverised coal through tuyeres into the blast furnace
JPH0255335B2 (en)
ES8202521A1 (en) Installation for conveying fine-grained material.
NO931189L (en) SEPTIC TANK INCLUDING GAS SUPPLEMENT SLAM CIRCULATOR
AU4935790A (en) Method for the pneumatic injection of metered quantities of powdered substances into a chamber at a variable pressure
GB981826A (en) Fluidizable solid injection system for furnaces
TW334507B (en) Process for the continuous conveying of a fine-grained and/or pulverized
GB1374211A (en) Method and apparatus for dispesning a fluidisable solid from a pressure vessel
AU603162B2 (en) Process for injecting, by pneumatic means, metered quantities of pulverulent material into a chamber which is under variable pressure
JPH07295654A (en) Water level control system for multi-branch tanks
NZ224650A (en) Programmable pump control
JPS5534761A (en) Flow rate changeover device
JPS5629084A (en) Operation control of pump
JPS5733719A (en) Controlling method of flow rate distribution for mixed fuel
JPS57201812A (en) Flow rate measuring device for molten slag
Elster et al. Sediment transport, depositional processes and particle bound elements of the Vaagaavatn delta, Norway
AU7717891A (en) Hydraulic safety and regulating system
SU818560A1 (en) Method of regulating water feed on rice irrigation system
JPS6425911A (en) Method and apparatus for controlling blowing quantity of fine powdered coal
JPS5675321A (en) Carrying device for pulverized substance under pressure