Valve Stand with Multi Orifice Mixer. Zone Control Malfunction. 3 Way Valve Malfunction. Mixing Degree Wave. Toyo-Sun Machinery Co., Ltd.

Similar documents
Series IRV1000/2000/3000

LECTURE 20 FLOW CONTROL VAVLES SELF EVALUATION QUESTIONS AND ANSWERS

Priority (Swing) Motors Data and Specifications

ENS-200 Energy saving trainer

INSTALLATION OPERATION MAINTENANCE

Portable Gas Monitor GX User Maintenance Manual (H4-0050)

The Compact, Portable, Efficient and Economical Solution to boost Shop Compressed Air Pressure by 2 or 3 times

REV0709. Parts List. Hydraulic Cylinder Model MODEL C SINGLE-ACTING, SPRING RETURN HYDRAULIC CYLINDER. Max. Capacity: 55.2 Tons at 10,000 PSI

WATER HYDRAULIC HIGH SPEED SOLENOID VALVE AND ITS APPLICATION

XDF BURNERS DUAL FUEL EXCESS AIR BURNER FEATURES DESCRIPTION EXCESS AIR OPERATION

M-System s I/P and P/I Transducers

No.IL02-OM00011-A PRODUCT NAME LOCK UP VALVE. MODEL/ Series IL201 IL211

Self-priming makes priming unnecessary Exhausts the air inside the suction pipe to suck up liquid. Air operated type.

Life Cycle Benefits: Maintenace (Control Valve Diagnostic and Field Device Diagnostic Management)

Max operation pressure 6kg/cm 2. Boost pressure rate Air pressure supply 5kg/cm Hydraulic fluid expelled l/min

MITIGATING PIPE AND RISER HYDRAULIC PIPELINE ISSUES WITH THE I-RISER PLUS

Vacuum Saving Valve Series ZP2V How to Order ZP2V A5 03 Connection thread symbol for the pad Male thread connection Symbol Thread Applicable fixed ori

Leak free Pipe Rupture Valve for Excavators

DC5A. Cyclone Separator Trap for Air. Copyright 2015 by TLV Co., Ltd. All rights reserved ISO 9001/ ISO MA-03 (DC5A) 19 June 2015

Exercise 2-3. Flow Rate and Velocity EXERCISE OBJECTIVE C C C

OWNER S TECHNICAL MANUAL

WATER HYDRAULIC SYSTEM FOR HIGH SPEED CYLINDER DRIVE

Maintenance and Troubleshooting of Pneumatic Conveying Systems for Sand in a Foundry

Economic Benefits Of Compressor Analysis >

Fisher DVI Desuperheater Venturi Inline

DFT Valves. Selecting Control Valves

THE INFLOW OF UNWANTED AIR

A STUDY ON THE ENTRAPPED AIR BUBBLE IN THE PLASTICIZING PROCESS

Discharge Relief Valve Operation & Maint.

Developments on Flow Rate And High Pressure Stability of Peroxide Dosing Pumps For The Chemical Industry

Composite Pistol-Type Air Needle Scaler OWNER S MANUAL

Automatic Non-freeze Valve NF6

PETROLEUM & GAS PROCESSING TECHNOLOGY (PTT 365) SEPARATION OF PRODUCED FLUID

ANTI SHOCK RELIEF VALVE

Waterous Relief Valve

MECHANICAL EQUIPMENTS: COMPRESSORS, PUMPS, SEALS, SPEED DRIVES, CONTROL VALVES & ACTUATORS & SAFETY RELIEF VALVES

Manual of SF6 Comprehensive Tester

AUTOMATIC GAS MANIFOLDS

Fluid Machinery Introduction to the laboratory measurements

- From 2005 year model, replacing with RM250 with 2-stroke engine, RM-Z450 with 4-stroke engine was introduced in the market. - From 2008 year model,

Operation Manual Air Saver Unit ASV5000 Series

RAM Operation Manual. Worldwide Manufacturer of Gas Detection Solutions

WW-730. Pressure Sustaining/Relief Control Valve

Chapter 2 Preparations for Tank Cleaning Work

15ME-014 INSTRUCTION MANUAL OF STERN TUBE SEALING TYPE EVK2RV. URL

Dry Gas Seal Rack CH-3185 Schmitten Tel Mail:

TECHNICAL BENEFITS OF CJS / RAISE HSP. Technical Advantages

RE / Meter out pressure compensator Sandwich plate design Type SCA... /Series 2X. Description of function, Section 1/6. Replaces: 09.

ACCU-MIX 1200 / / 26270

Flow meter. bellow vaporizer. APL valve. Scavenging system

Techniques for measuring Spray drift

Plant Air Energy Saving

Courses of Instruction: Controlling and Monitoring of Pipelines

Impact of imperfect sealing on the flow measurement of natural gas by orifice plates

Plant design and control valve selection under increasing cost and time pressure - Part I

ANNEX AMENDMENTS TO THE INTERNATIONAL CODE FOR FIRE SAFETY SYSTEMS (FSS CODE) CHAPTER 15 INERT GAS SYSTEMS

Detector Carrier Gas Comments Detector anode purge or reference gas. Electron Capture Nitrogen Maximum sensitivity Nitrogen Argon/Methane

Model: 43T. Bermad Pressure Relief Valve

13. Evaporative Emission Control System

INTENDED USE TECHNICAL SPECIFICATIONS

Unit 24: Applications of Pneumatics and Hydraulics

OPERATING INSTRUCTIONS Pressure Control System PCS-20 through PCS-100

Lecture 19 PRESSURE-CONTROL VALVES [CONTINUED]

Ruskinn Hypoxia and Anoxia Workstations. innovation in incubation

Multi-chambered volume synchroniser Type MZB

The Ins and Outs of I/P Transducers

RAM Operation Manual. Worldwide Manufacturer of Gas Detection Solutions

Coriolis Mass Flow Meter

User s Manual. Digital micro pipette for liquid handling CERTIFIED ISO9001

Annual Report on Liquefied Petroleum Gas (LPG) Related Accidents

TECHNICAL DATA. Low-Flow Foam Preaction System with Hydraulically Actuated Concentrate Control Valve.

Experimental Verification of Integrated Pressure Suppression Systems in Fusion Reactors at In-Vessel Loss-of -Coolant Events

Figure 4 Figure 5 Figure 6

Drilling Efficiency Utilizing Coriolis Flow Technology

MANUAL GAS MANIFOLDS

RAM 4021-PR. Operation Manual. Worldwide Manufacturer of Gas Detection Solutions

FUNDAMENTAL SAFETY OVERVIEW VOLUME 2: DESIGN AND SAFETY CHAPTER I: AUXILIARY SYSTEMS. A high-capacity EBA system [CSVS] [main purge]

FLUID POWER FLUID POWER EQUIPMENT TUTORIAL ACCUMULATORS. This work covers part of outcome 2 of the Edexcel standard module:

Vibration and Pulsation Analysis and Solutions

RARS5000 AIR BODY SAW OWNER S OPERATING MANUAL

TECHNICAL DATA. than the water inlet pressure to the concentrate

MZX. Three-Port Seat Valves SPECIFICIATIONS AND GUIDE TO SELECTION

Introduction. Part one: Identify the Hydraulic Trainer Components

Tech Tips. Service Call: Adjustable Hydraulic Valves Flow controls Pressure controls Sequence valves Holding valves

The benefits of system solutions for valve users

Lab 3 Introduction to Quantitative Analysis: Pumps and Measurements of Flow

APPENDIX B TESTING PROTOCOLS. Method A: Straight Test Method B: Angular Deflection Test. Method C: Shear Load Test

Agilent ICP-MS Interactive Troubleshooting tool for Low sensitivity

Description. Chassis. Cabinet. Long chassis - Type: Dimensions (mm): 2700 x 1200 x 1678

IBEDA GAS MIXERS HIGHEST PRECISION FOR YOUR WELDING AND CUTTING PROCESSES

LAKOS Waterworks. PWC Series Sand Separators. Installation & Operation Manual LS-829 (10/12)

RAM 4021-DPX Operation Manual

L-14 Fluids [3] Fluids in Motion Fluid Dynamics Hydrodynamics Aerodynamics

CLASS D - SENSITIVE LEAK TEST GAS AND BUBBLE METHOD. 1.1 To provide definitive requirements for PNEUMATIC pressure testing of piping systems.

Fig. 1: Mechanical vacuum gauge (left) and capacitive vacuum gauge (right)

Elevator Concepts ltd. by Wurtec Krause Riverview, MI Fax:

Blue River Technologies Port-A-Poly Mixer w/2.5 GPH LMI Pump And Secondary Water Dilution Line INSTALLATION AND OPERATION

Needle valve. Contents. User s Manual. (1) Be sure to read the following warranty clauses of our product 1. (2) General operating instructions 2

DESIGN DATA OBSOLETE. C. Inspections - It is imperative that the system be inspected and tested on a regular basis. See Inspection

Xpress L90LS Directional Control Valve. Catalog HY /UK December, 2001

Transcription:

Valve Stand with Multi Orifice Mixer Zone Control Malfunction 3 Way Valve Malfunction Mixing Degree Wave Toyo-Sun Machinery Co., Ltd.

On this occasion, our company has developed the Online Digital Hot Rolling Oil System with NEVI system. This system secures the oil s maximum plate-out to the roll by using multi orifice mixers, and optical technology for each mixing degree according to the density. features 1. Mixing degree digitalization 2. Most suitable plate out 3. Early warning of suffocation factor 4. Oil consumption cut 1.Summary The effectiveness of the hot rolling oil is greatly affected by the density and the mixing degree (the degree of water and oil mixing condition). To obtain an optimum mixing degree, first, it is necessary to adjust the mixing degree with the multi orifice mixer. Then, the relationship between the oil s plate-out to the roll and the transparency number by density have to be obtained by using optical technology that expresses numerically the transparency number of the solution. According to the results of this, the mixing degree appropriate to obtain the maximum plate-out to the roll can be regulated online. Our company s system is a hybrid system comprised of a multi orifice mixer and a digital sensor. 90 / Stroke 2.Oil and Water Mixing (Injection Mixer) As shown in FIG.1, the Injection Mixer is comprised of an orifice and a diffusion chamber, and it is one of the most important devices in the rolling oil system to get the oil and water mixed. If the orifice s diameter is small, the solution will be well mixed. If the orifice s diameter is big, the water and oil will run into the nozzle headers in a separated state. According to the plate s width the nozzles of both sides will change to [wide], [middle], and [narrow]. If the spray is stopped, the quantity of water will change and as a consequence, the water and oil mixing condition will change and thus alter the oil s plate-out to the roll. The Online Digital System developed by our company, combined with the multi orifice mixer, is able to secure the maximum plate-out efficiency of the oil. FIG.1 Orifice Diffusion Room room Emulsion Exit 0.5 Orifice 1

3. Characteristics and FIG.2 Operating Principles In FIG.2, the basic principles of the optical-technology-using Online Digital System are shown. First, the water and oil mixing degree is numerically represented by the transparency number. If its density is high and it is well-mixed, the light will not pass through the solution easily; but, if its density is low and it is not well-mixed the transparency number will increase. The density is numerically represented by using the light reflected in the oil s particles. The density and mixing degree can be measured at the same time by taking a sample of the emulsion in the square-shaped cells. From the nozzle headers shown in FIG. 1, extract a sample of emulsion with the square-shaped cells. Then, obtain its numerical value using the portable kit D DKIT II and create a list of transparency number by density (as shown in Table 1). At the same time, prepare a test plate (square of 100 mm ) for each nozzle spray, and measure the oil s plate-out in each nozzle. If there is too much plate-out variation between each test plate it is because of bad mixing, in that case reduce the size of the multi orifices. If the size of the orifices is too small, plate-out variation will disappear in each nozzle, but the plate-out will also decrease. An appropriate range shows TABLE 1 which is permissible between ±5%. This value varies depending on each the density and type of each oil. If the water temperature is high, it might mix too much causing a decrease in the transparency number and in the plate-out. The values shown in TABLE 1 represent the maximum plate-out possible. A maximum plate-out can be obtained with minimum oil consumption and keeping variations limited. Transparency number 濃度別透過線数表 according to density TABLE 1 0.1 % 0.3 % 濃度 :(0.1%) 濃度 :(0.3%) 0.5 % 濃度 :(0.5%) 0.8 % 濃度 :(0.8%) 1.0 % 濃度 :(1.0%) 4.Objective Until now, hot rolling oil systems efficiency has been judged by their draft decrease rate of the rolling force. The decrease rate s amount has been controlled only by high/low densities for many years. However, recently many researches and experiments have found that the mixing degree has a great influence not only on the draft decrease rate, but also on the plate shape and its quality, proving this way the importance of the measurement of the mixing degree. The mixing degree may vary even though the density is the same because of other factors such as the water temperature and hardness. Also, after the sample is taken, the oil and water separate as time passes making the measurement of mixing degree impossible. The objective of our Online Digital System is to measure the mixing degree online and quantify it numerically. In addition, by detecting with the online sensor small infiltrations of oil in the carrier water when off-loading, accidents such as slips of the strip and biting failures can be avoided. 2

Air pilot FIG.3 Super thin combined header Water wrapping 3 Online direct sensor Air solenoid unit S.V unit Auto multi orifice mixer Rack & pinion type air cylinder 4 Reducing valve Check valve 3way valve 1 Valve stand Relief valve Flow meter Water pump Oil pump 2NEVI SYSTEM OHRO 回路図 Heater 5 Oil metering and water pump unit ONLINE DIGITAL SYSTEM CIRCUIT DIAGRAM Composition The Online Digital System can be divided broadly in 5 parts: 1 Valve stand with built-in multi orifice mixer 2 NEVI system, 3 Online Direct sensor, 4 D D KIT II, 5 Oil metering and water pump unit Hindrance causes with related information Part Ⅰ The following items all lead up to strip quality deter 10 ration or a big trouble Toyo-Sun online digital system with NEVI system can grip visually suffocation factors to proper hot rolling oil system. By digital or the board of pictures in the operator room. 1.Nozzle clogging 6.Water flow rate change by caused by pressure change 2 Nozzle deterioration 7.Change of density and mixing degree 3.Unbalance of density between 8.Change of density actuating Top & Bottom rolls sprayed defect of valve 4.Unbalance of mixing degree 9. Intermix of oil into spray between Top & Bottom rolls sprayed line caused by defect of 3way valve when off rolling 5. Metering pump deterioration 10.Pipe constriction 11.Defective water seal 12.Change of amount of plate out caused by water temperature 13.Defective zone control b dividing valves Toyo-Sun Machinery Co., Ltd. 1-1-19, Matsugashima-nishi, Ichihara-shi, Chiba, 290-0036 Japan TEL 0436-25-6411 FAX 0436-25-6414 URL http://www.toyo-sun.com/ Distributor: 3 100127

Blind spots to conventional hot rolling oil system 1.Heavy reliance on density control 2.Excessive dependence on rolling force 3.Disregard of water quality & quantity control 4.Excessive expectation on the oil type 5.Desregard of zone control 6. Poor interest in oil consumption 7.Disregard of the importance of water seals NEVII Syysstteem Deessccrri ipptti ioon & Feeaatturreess A. The NEVI system helps us identify the cause that hinders proper rolling oil. As shown in FIG. 1, the waves of each type of parameter and the optimum standard degree of mixing with some allowance are displayed on the screen. We take the degree of mixing wave as a standard, and in case there are protruding actual waves, the system s computerized process shows abnormal signals through images that tell us which factor is causing the problem. Normal Condition Rolling force reduction wave FIG. 1 Actual degree of mixing wave Optimum standard degree of mixing wave 1 2 3 4 5 6 7 Plate temperature Water pressure Water temperature Water quantity Oil quantity Density 3-way valve 1 2 3 4 5 6 7 B. FIG2 shows us an actual wave protruding from the standard wave. In part (A) of the image the continuous line protrudes left from the optimum standard degree of mixing; this shows us that for some reason, the water and oil are over-mixing, the light s transparency number is small, and the plate-out is going down. Contrariwise, in wave (B) we can see that the water quantity is diminishing due to nozzle clogging and this is increasing the water temperature affecting the water-oil mixing. Thus, oil s plate-out variations become a matter of concern. Part (C) shows us oil infiltration in the water spray during off-rolling. There s a possibility that the next plate entering will slip. Abnormal Condition1 FIG. 2 Nozzle deterioration high water temperature water/oil pump malfunction Nozzle clogging low water temperature water/oil pump malfunction Oil infiltration in the water Transparency Number (Degree of Mixing) C. FIG.3 is an example of a poor zone control and 3-way valve malfunctioning. The valve in charge of the zone control leaks, increasing the water flow rate, and thus changing the degree of mixing. The water and oil over-mix and make the actual wave to protrude left from the standard wave as shown in (A). In (B) we see that even though a normal electric given to 3-way valve, in case the wave is corrupted, an alarm signal that indicates that the 3-way valve is not working properly is produced. Zone control malfunction Abnormal Condition2 3-way valve malfunction FIG 3 Transparency Number (Degree of Mixing)

D. FIG.4 is an example where water seal malfunction is suspected. Due to a continuous leak of coolant water, the rolling force reduction rate becomes lower everything but the rolling force reduction wave is normal, and a wave similar to the one in FIG.4 is formed. In other words, the line that was supposed to be reduced until the original wave becomes the actual line. Abnormal Condition3 Rolling force reduction wave FIG 4 Actual degree of mixing wave Optimum standard degree of mixing wave 1 2 3 4 5 6 7 Plate temperature Water pressure Water temperature Water quantity Oil quantity Density 3-way valve 1 2 3 4 5 6 7 Attention: The NEVI system stands for, Navigator, Evaluate, Visual, Indicator. Our system uses a degree of mixing wave with a certain range as a navigator; it permit us visualize the degree of mixing in the form of a continuous line, and in case it protrudes from the determined range it helps us evaluate the degree of mixing. E. Example of Part Ⅱ: Factors that hinder an optimum rolling oil a.nozzle Clogging A total flow rate reduction of 0.8% in the header, and a change of 200 units in degree of mixing can be detected. FIG 5 Degree of mixing value: 4000 (Flow rate of nozzle #2:4.3l/min) The throttle valve closes gradually Degree of mixing value : 4200 ( Flow rate of nozzle #2:4.0l/min ) B.Nozzle Deterioration A total flow rate increase of 1.6% in the header, and a change of 200 units in degree of mixing can be detected. Degree of mixing value : 4000 ( Flow rate of nozzle #2:4.3l/min) The throttle valve opens gradually Degree of mixing value : 3800 ( Flow rate of nozzle #2:4.9l/min)