Line types and thicknesses


The standard ISO 128:1982 gives 10 line types that are defined A to K (excluding the letter I). The table in Figure 3.4 shows these lines. The line types are 'thick', 'thin', 'continuous', 'straight', 'curved', 'zigzag', 'discontinuous dotted' and 'discontinuous chain dotted'. Each line type has clear meanings on the drawing and mixing up one type with another type is the equivalent of spelling something incorrectly in an essay. The line thickness categories 'thick' and 'thin' (sometimes called 'wide' and 'narrow') should be in the proportion 1:2. However, although the proportion needs to apply in all cases, the individual line thicknesses will vary depending upon the type, size and scale of the drawing used. The standard ISO 128:1982 states that the thickness of the 'thick' or 'wide' line should be chosen according to the size and type of the drawing from the following range: 0,18; 0,25; 0,35; 0,5; 0,7; 1; 1,4 and 2mm. However, in a direct contradiction of this the standard ISO 128-24:1999 states that the thicknesses should be 0,25; 0,35; 0,5; 0,7; 1; 1,4 and 2mm. Thus confusion reigns and the reader needs to beware! With reference to the table in Figure 3.4, the A-K line types are as follows. The ISO type 'A' lines are thick, straight and continuous, as shown in Figure 3.5. They are used for visible edges, visible outlines, crests of screw threads, limit of length of full thread and section viewing lines. The examples of all these can be seen in the vice assembly detailed drawings. These are by far the most common of the lines types since they define the artefact. The ISO type 'B' lines are thin, straight and continuous, as shown in Figure 3.6. They are used for dimension and extension lines, leader lines, cross hatching, outlines of revolved sections, short centre lines, thread routes and symmetry ('equals') signs. 

Engineering Drawing for Manufacture
by Brian Griffiths
· ISBN: 185718033X
· Pub. Date: February 2003
· Publisher: Elsevier Science & Technology Books


 

Manufacturing Data and Knowledge


Machining methods (also referred to as machining practices) provide CAPP with the knowledge, expertise, and procedures that a human process planner uses. These methods may be based on sound scientific principles, experimental results, experience, or preferences established within a particular machining context. They also may be generic and applicable over a wide range of machining problems or specific to a single one. The challenges in using machining methods within CAPP fall into the following categories: • Identification and retrieval • Implementation • Maintenance • Customization Identification and retrieval are concerned with understanding how a human process planner applies experience and techniques to make decisions when generating process plans: What decisions are being made? What characteristics of the situation are being recognized by the planner that trigger these decisions? The main challenge here stems from the fact that human planners do not necessarily follow a consistent strategy in applying methods. The process often requires complex trade-offs of information from several sources. When one of these sources is experience, the basis of the applied method can be difficult to verify. Thus, identification and retrieval of methods are not just a bookkeeping task. Rather, it requires the cultivation of an attitude toward process planning based on a sound methodology for applying machining methods. Methods implementation requires an approach that is general enough to capture information from very different sources while at the same time is simple enough to provide a maintainable, noncorruptible environment. Rule-based expert systems have been the most commonly adopted implementation strategy among CAPP system developers. Because the need to update or add new methods always exists as more information becomes available or as new methods are applied to more applications, maintenance of the knowledge base becomes a key concern. As changes are made, the integrity of the information needs to be preserved. One problem occurs when new methods are added that conflict with old ones. The system needs to include a strategy for resolving such conflicts. One approach that has been used extensively with expert systems is to place the onus on a knowledgable engineer to avert such problems. However, as the size of the knowledge base grows, the cost of employing dedicated personnel for this task becomes prohibitive. Finally, creating off-the-shelf CAPP systems with the methods included is a difficult if not impossible task. This is because it is unlikely that the system developer can capture all the desired methods from all potential users during system development. Thus, while a system may come with some generic, widely accepted methods, it must include a facility to allow new methods customized to each context to be added to the system.

THE MECHANICAL
SYSTEMS
DESIGN
HANDBOOK
Modeling, Measurement,
and Control
OSITA D. I. NWOKAH
YILDIRIM HURMUZLU
Southern Methodist University
Dallas, Texas
CRC PRESS
Boca Raton London New York Washington, D.C.

BASIC LINKAGE CONCEPTS

Kinematic Elements A linkage is composed of rigid-body members, or links, connected to one another by rigid kinematic elements, or pairs. The nature of those connections as well as the shape of the links determines the kinematic properties of the linkage. Although many kinematic pairs are conceivable and most do physically exist, only four have general practical use for linkages. In Fig. 3.1, the four cases are seen to include two with one degree of freedom (f = 1), one with f = 2, and one with f = 3. Single-degree-of-freedom pairs constitute joints in planar linkages or spatial linkages. The cylindrical and spherical joints are useful only in spatial linkages. The links which connect these kinematic pairs are usually binary (two connections) but may be tertiary (three connections) or even more.A commonly used tertiary link is the bell crank familiar to most machine designers. Since our primary interest in most linkages is to provide a particular output for a prescribed input, we deal with closed kinematic chains, examples of which are depicted in Fig. 3.2. Considerable work is now under way on robotics, which are basically open chains. Here we restrict ourselves to the closed-loop type. Note that many complex linkages can be created by compounding the simple four-bar linkage.This may not always be necessary once the design concepts of this chapter are applied. 
Richard E. Gustavson

Technical Staff Member
The Charles Stark Draper Laboratory, Inc.
Cambridge,Massachusetts
Downloaded from Digital Engineering Library @ McGraw-Hill (www.digitalengineeringlibrary.com)

 

Standard Test Method for Water and Sediment in Crude Oil by Centrifuge Method

This standard is issued under the fixed designation D 96; the number immediately following the designation indicates the year of original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A superscript epsilon (e) indicates an editorial change since the last revision or reapproval. This method has been approved by the sponsoring committees and accepted by the Cooperating Societies in accordance with established procedures. This test method has been adopted for use by government agencies to replace Method 3003 of Federal Test Method Standard No. 791b. Annex A1 is under revision and will be included in subsequent revisions to this standard. 1. Scope 1.1 This test method covers the centrifuge method for determining sediment and water in crude oil during field custody transfers. This test method may not always provide the most accurate results, but it is considered the most practical method for field determination of sediment and water. When a higher degree of accuracy is required, the laboratory procedure described in Test Methods D 4006, D 4377 or D 473 should be used. NOTE 1—Water by distillation and sediment by extraction are considered the most accurate methods of determining sediment and water in crude oils. As such, these methods should be employed to resolve differences in results from variations of this procedure or between this procedure and other methods, or in the case of a dispute between parties. 1.2 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use. 2. Referenced Documents 2.1 ASTM Standards: D 235 Specification for Mineral Spirits (Petroleum Spirits) (Hydrocarbon Drycleaning Spirits)2 D 362 Specification for Industrial Grade Toluene2 D 473 Test Method for Sediment in Crude Oils and Fuel Oils by the Extraction Method3 D 846 Specification for Ten-Degree Xylene2 D 1209 Test Method for Color of Clear Liquids (Platinum- Cobalt Scale)2 D 3699 Specification for Kerosine4 D 4006 Test Method for Water in Crude Oil by Distillation4 D 4057 Practice for Manual Sampling of Petroleum and Petroleum Products4 D 4177 Practice for Automatic Sampling of Petroleum and Petroleum Products4 D 4377 Test Method for Water in Crude Oils by Potentiometric Karl Fischer Titration4 E 1 Specification for ASTM Thermometers5 E 542 Practice for Calibration of Volumetric Ware6 2.2 API Standards:7 Manual of Petroleum Measurement Standards Chapter 8, Sampling Petroleum and Petroleum Products Chapter 10, Sediment and Water 3. Summary of Test Method 3.1 Known volumes of crude oil and solvent (water saturated if required) are placed in a centrifuge tube and heated to 60°C 6 3°C (140°F 6 5°F). After centrifugation, the volume of the sediment-and-water layer at the bottom of the tube is read. NOTE 2—It has been observed that for some waxy crude oils, temperatures of 71°C (160°F) or higher may be required to melt the wax crystals completely so that they are not measured as sediment. If temperatures higher than 60°C (140°F) are necessary to eliminate this problem, they may be used with the consent of the parties involved. If water saturation of the solvent is required, it must be done at the same temperature. 4. Significance and Use 4.1 A determination of sediment and water content is required to determine accurately the net volumes of crude oil involved in sales, taxation, exchanges, inventories, and custody transfers. An excessive amount of sediment and water in crud.
---------------------
1 This test method is under the jurisdiction of Committee D-2 on Petroleum
Products and Lubricants and is the direct responsibility of Subcommittee
D02.02.OB on Sediment and Water (Joint ASTM-JP).
Current edition approved March 25, 1988. Published December 1988. Originally
published as D 96 – 63T. Last previous edition D 96 – 73 (1984).e1
2 Annual Book of ASTM Standards, Vol 06.04.
3 Annual Book of ASTM Standards, Vol 05.01.
4 Annual Book of ASTM Standards, Vol 05.02.
5 Annual Book of ASTM Standards, Vol 14.03.
6 Annual Book of ASTM Standards, Vol 14.02.
7 Available from American Petroleum Institute, 1220 L St., Northwest, Washington,
DC 20005.

An American National Standard
British Standard 4385
American Association State
Highway Transportation Standard
AASHTO No. T55

AMERICAN SOCIETY FOR TESTING AND MATERIALS
100 Barr Harbor Dr., West Conshohocken, PA 19428
Reprinted from the Annual Book of ASTM Standards. Copyright ASTM