1. Trang chủ
  2. » Kinh Tế - Quản Lý

ASTM D216 -77 (1982) Method of Test for Distillation of Natural Gasoline (Withdrawn 1988)

4 2 0

Đang tải... (xem toàn văn)

THÔNG TIN TÀI LIỆU

Thông tin cơ bản

Tiêu đề Method of Test for Distillation of Natural Gasoline
Năm xuất bản 1982
Định dạng
Số trang 4
Dung lượng 307,08 KB

Nội dung

T h e bottle shall be closed immediately with a tight- fitting stopper, and placed in an ice bath or refrigerator capable of bringing the gasoline to a temperature of not less than 32°F

Trang 1

9009276 0019816 8 T 5 =

Designation: D 216 - 77 (Reapproved 1982)

4Ib

Designation: 191 /65 (75)

An American National Standard British Standard 4717

Standard Method for

This standard is issued under the fixed designation D 216; 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 This is also a standard of the Institute of Petroleum issued under the fixed designation IP 19 I The final number indicates the year of last revision

This method was issued as a joint A S T M - I P standard in 1965

This method has been adopted f o r use by government agencies to replace Method 1015 of Federal Test Method Standard No

791 b

1 Scope

1.1 This method covers the distillation of

natural gasoline

NOTE 1-The values stated in inch-pound units

are to be regarded as the standard

2 Applicable Documents

2 1 ASTM Standards:

E 1 Specification for ASTM Thermometer?

E 133 Specification for Distillation Equip-

ment’

3 Summary of Method

3 1 A sample of 1 0 0 ml is distilled at at-

mospheric pressure without fractionation, and

readings are taken of the vapor temperatures

corresponding t o the amounts distilled

4 Significance

4 1 Natural gasoline is so volatile that it

must b e handled, measured, condensed, and

recovered at lower temperatures than most

petroleum products This method incorpo-

rates handling and other precautions for pre-

cision

4.2 A n indication of the volatility blending

characteristics that a natural gasoline will ex-

hibit when blended with refinery stocks t o

make a finished gasoline is obtained from the

results of this type of distillation

5 Apparatus

5 1 T h e apparatus listed in the following,

5 1 1 through 5 1 5 , shall conform to Specifi-

cation E 133

flask

5.1.1 Flask -Standard 100-ml distillation

5.1.2 Condenser and Cooling Bath

5.1.3 Shield, Type 1 o r 2

5.1.4 Flask Support, Type 1 or 2 with 5.1.5 Graduared Cylinder, 1 00-ml

structed that heat can be obtained to distill the product at the rate specified T h e flame shall never be so large that it spreads over a circle

of diameter greater than 4’/2 in (1 1 5 mm) on the under surface of the asbestos board A

sensitive regulating valve and gas pressure governor are desirable adjuncts, as they give complete control of heating

5.1.7 Electric Heater - An electric heater may be used instead of the gas burner and shall b e capable of bringing over the first d r o p within the time specified in 8.1 when started cold, and of continuing the distillation at a

uniform rate (A heater unit of low-heat ca- pacity, adjustable from O to 750 W , has been found satisfactory) When an electric heater is employed, the portion of the shield above the board Type A

This method is under the jurisdiction of ASTM Committee D-2 on Petroleum Products and Lubricants

In the IP this method is under the jurisdiction of the Stan- dardization Committee

Current edition approved Aug 26 1977 Published October

1977 Originally published as D216-25 Last prexious edition

.4miral Book oj’ASTM Slandards, Vols 05.03 and 14.01

Iwiirol Book ofAS7’M Standards Vols 05.03 and 14.02 D216-54 (1976)

NOTICE: This standard has either been superseded and replaced by a new version or discontinued

Contact ASTM International (www.astm.org) for the latest information

Trang 2

W 900927b 0019817 731 =

D 2 1 6 - @ 191

board shall be the same as with the gas

burner, but the part below the board may be

omitted

shown below and conforming to the require-

ments for ASTM Thermometer 7 F o r 7 C , as

prescribed in Specification E 1, or IP ther-

mometer 5 C

Thermometer Number Temperature Range ASTM IP

30 to 580°F 7F

6 Sampling

6.1 Samples should be collected in a previ-

ously cooled bottle, preferably by immersing

the bottle in the liquid, where possible, and

discarding the first sample Where immersion

is not possible the sample should be drawn off

into a previously cooled bottle in such a man-

ner that agitation is kept at a minimum T h e

bottle shall be closed immediately with a tight-

fitting stopper, and placed in an ice bath or

refrigerator capable of bringing the gasoline

to a temperature of not less than 32°F (O'C),

nor more than 40°F (4.5"C)

7 Preparation of Apparatus

7.1 Fill the condenser bath with cracked

ice (Note 2) and add enough water to cover

the condenser tube Maintain the temperature

between 32 and 34°F (O and 1.1"C) Agitation

with air gently aids in maintaining the re-

quired temperature range

NOTE 2 -Any other convenient cooling medium

may be used

7.2 Swab the condenser tube to remove

any liquid remaining from the previous test A

piece of soft, lint-free cloth attached to a cord

o r copper wire may be used for this purpose

7 3 Measure a 100-ml sample in the 100-

ml graduated cylinder at 32 to 40°F (O to

4.5"C) and transfer it directly to the distil1.a-

tion flask Both the flask and the graduated

cylinder shall have been cooled t o a tempera-

ture of from 32 to 40°F (O to 4.5"C) before

use Do not permit any of the liquid to flow

into the vapor tube

7 4 Make a record of the room tempera-

ture at the time of each distillation T h e heat-

ing apparatus including the shield and flask

support shall be at room temperature at the

start of each distillation

7.5 Fit the thermometer (previously cooled

to a temperature of 32 to 40°F (O to 4.5"C)

and dried) tightly into the flask with a suitable cork so that it will be in the middle of the neck, and so that the lower end of the capil- lary tube is on a level with the inside of the bottom of the vapor outlet tube at its junction with the neck of the flask

7.6 Place the charged flask in the 11/4-in (32-mm) opening in the 6 by 6-in (150 by 150-mm) asbestos board with the vapor outlet

tube inserted into the condenser tube A tight

connection must be made by means of a cork through which the vapor tube passes Adjust the position of the flask so that the vapor tube extends into the condenser tube not less than

1 in (25 mm) nor more than 2 in (50 mrn) 7.7 Place the graduated cylinder used in measuring the charge without drying, at the outlet of the condenser tube in such a position that the condenser tube shall extend into the cylinder at least 1 in (25 m m ) , but not below the 100-ml mark Immerse the graduated cyl- inder up to the level of the outlet of the condenser tube in a transparent bath main- tained between the temperatures of 32 and 34°F (O and 1.i"C) Cover the top of the cylinder closely during the distillation with a piece of blotting paper, or its equivalent, so

cut as to fit the condenser tube tightly A lead washer, or other suitable material, resting on

the blotting paper is a convenient accessory as

it serves to hold the paper tightly against the top of the cylinder and also provides the addi- tional weight necessary t o overcome the buoy- ant effect of the liquid in the cooling bath

8 Procedure

8.1 When everything is in readiness, apply heat immediately at a uniform rate, so regu- lated that the first drop of the condensate falls from the condenser in notless than 2 min nor more than 5 min When the first drop falls from the end of the condenser, move the re- ceiving cylinder so that the end of the con- denser tube shall touch the side of the cylin- der Then regulate the heat so that the first 10

ml of distillate shall be recovered in not less than 3 min nor more than 4 min Thereafter, maintain the rate of distillation uniformly at not less than 4 rnl/min nor more than 5 rnl/ min Record the reading of the distillation thermometer when the level of the distillate

Trang 3

7009276 O O L 9 8 L 8 678 9

D 2 1 6 - @ 191

rated at the temperature in question Make clear distinction between the inclusion or ex- clusion of the distillation loss figure in the report of the volume of distillate obtained a t

a n y prescribed temperature In the first case report the figure as the volume ewporared, in

the second, as the volume recovered

reaches each 10-ml mark on the cylinder I n

case a product is being tested to ascertain

whether or not i t conforms with a given speci-

fication, make and record all necessary obser-

vations, whether or not they are included in

the series ordinarily employed by the labora-

tory making the test

8.2 When the liquid residue in the distilla-

tion flask is approximately 5 m l , the heat may

be increased because of the presence of heavy

ends which have relatively high boiling points

However, do not apply any further increase of

heat after this adjustment T h e 4 to 5-ml rate

cannot always be maintained from this point

to t h e end of the distillation, but in no case

should the period between the point when

approximately 5 ml of the liquid remains i n

the flask and the end point be more than 5

min

8 3 Continue the heating until the mercury

reaches a maximum and starts to fall consist-

ently after the bottom of the flask has become

dry Record the highest temperature observed

on the distillation thermometer as the maxi-

mum temperature or erid poirir

8 4 Observe the total volume of the distil-

late collected in the receiving cylinder at the

conclusion of the distillation, and thereafter at

not less than ?-min intervals, until successive

observations agree Then record this volume

as the recover!

8.5 Pour the cooled residue from the flask

into a small cylinder graduated in 0.1 m l ,

measure when cool, and record the volume as

residrre at 32 to 40°F (O to 4.5"C)

8.6 Calculate the difference between 100

ml and the sum of the recovery and the resi-

due and record as disrillariori loss

NOTE 3 - A b n o r m a l distillation losses, when

caused by low barometric pressure, may be cor-

rected by the equation given below to an approxi-

mation of the loss to b e expected under normal

pressure The corrected losses shall not be used in

the calculation of percentages e v a p o r a t e d

Corrected loss = A L + B

where:

L = observed distillation loss,

A and B = empirical constants, as given in Table

1, for various values of t h e observed baromet-

ric pressure

8.7 The sum of the volunie collected in the

cylinder at any specified temperature, includ-

ing the initial boilins point, and the distillation

loss may be recorded as the percentage evapo-

9 Correction of Temperature Points to Stan-

9 1 Ascertain and record the actual baro- metric pressure, but do not make any correc- tion except in case of dispute I n such cases correct the temperature points to 760 mm (29.92 in.) Hg, by the use of the Slrdney Young equation, as follows:

For Celsius readirrgs:

For F d i reri h eir readings:

where:

C, and C, = the correction to be added to the observed temperature t , or I,, respec- tively, and

P = the actual barometric pressure, m m Hg

I n case of dispute, however, no test shall be regarded as official when conducted under an absolute pressure lower than 735 m m (38.94 in.) Hg

9.2 The following table is a convenient ap- proximation of the corrections as calculated

by the above equation:

dard Atmospheric Pressure

C, = 0.00012 (760 - P ) ( 2 7 3 + I , )

C, = 0.00012 (760 - P)(160 + I,)

Temperature Range

"C "F

10 to 30 50 to 86

30 to 50 86 to 122

50 to 70 122 to 158

70 to 90 158 to 194

90 to 110 194 to 230

110 to 130 230 to 266

130 to 150 266 to 302

150 to 170 302 to 338

170 to 190 338 to 374

190 to 210 374 to 410

210 to 230 410 to 446

230 to 250 446 to 482

250 to 270 482 to 518

270 to 290 518 to 554

290 to 310 554 to 590

Correction"ll0-mm Difference in Pressure

"C "F

0.35 0.63 0.38 0.68 0.40 0.77 0.47 0.76 0.45 0.81 0.47 0.85 0.50 0.89 0.52 0.94 0.54 0.98 0.57 1 o2 0.59 1 .O6

0.62 1.11 0.61 1.15 0.66 1.19 0.69 1 ?-I

" To be added in case barometric pressure is below 760

m m Hg (101.3 kPa); to be subtracted in case barometric pressure is above 760 m m Hg (101.3 kPa)

Trang 4

= 900927b O O l 9 8 ~ 9 5 0 4

D 2 1 6 - @ 191

pressure and report that the correction has been made Do not correct thermometer readings for errors due to emergent stem

11 Precision

11.1 With proper care and strict attention

to details, duplicate results obtained for end point should not differ from each other by more than 6°F (3.5"C) Differences in dupli- cate temperature readings for each prescribed percentage point should not exceed the amounts equivalent to 2 ml of distillate at each point in question

Correction io-mm Temperature Range Difference in Pressure

"C "F "C "F

310 to 330 590 to 626 0.71 1.28

330 to 350 626 to 662 0.74 1.32

350 to 370 662 to 698 0.76 1.37

370 to 390 698 to 733 0.78 1.31

390 to 410 734 to 770 0.81 1.45

10 Report

10.1 Report the data recorded in Section 8

according to requirements, the room temper-

ature, and the barometric pressure I n cases of

dispute, correct for variations of barometric

TABLE 1 Values of the Constants "A" and "B" Used in

Obtaining Corrected Distillation Loss

Pressure Pressure

mm HE mm He

B

Barometric A Barometric A

560 0.231 0.384 660 0.375 0.312

570 0.240 0.380 670 0.400 0.300

580 0.250 0.375 680 0.428 0.286

590 0.261 0.369 690 0.461 0.269

600 0.273 0.363 700 0.500 0.250

610 0.286 0.357 710 0.545 0.227

620 0.300 0.350 720 0.600 0.200

630 0.316 0.342 730 0.667 0.166

640 0.333 0.333 740 0.750 0.125

650 0.333 0.323 750 0.857 0.071

760 1.000 0.000

The American Society f o r Testing and Muterials takes no position respecting the validity of any patent rights asserted in

connection with any item mentioned in this standard Users of this standard are expressiv advised that determination of the va1idit.v

of any such patent rights, and the risk of infringement of such rights, are entirely their own responsibility

This standard is subject to revision at any time b,v the responsible technical committee and must be reviewed every five ?ears and i f not revised, either reapproved or withdrawn Your comments are invited either for revision of this standard or f o r additional standards and should be addressed to A S T M Headquarters Your comments will receive careful considerationat a meeting of the

responsible technical commitlee which you ma-v attend I f you feel that your comments have not received afair hearingyou should makeJour views known to the A S T M Committee on Standards, 1916 Race SI., Philadelphia, Pa 19103

Ngày đăng: 10/03/2024, 13:57

TỪ KHÓA LIÊN QUAN

TÀI LIỆU CÙNG NGƯỜI DÙNG

TÀI LIỆU LIÊN QUAN