AU6576880A - Creación de Inventos y Patentes con Inteligencia Artificial

AU6576880A – Method for continuously determining the composition and mass flow of a slurry
– Google Patents

AU6576880A – Method for continuously determining the composition and mass flow of a slurry
– Google Patents
Method for continuously determining the composition and mass flow of a slurry

Info

Publication number
AU6576880A

AU6576880A
AU65768/80A
AU6576880A
AU6576880A
AU 6576880 A
AU6576880 A
AU 6576880A
AU 65768/80 A
AU65768/80 A
AU 65768/80A
AU 6576880 A
AU6576880 A
AU 6576880A
AU 6576880 A
AU6576880 A
AU 6576880A
Authority
AU
Australia
Prior art keywords
slurry
butter
content
continuously
value
Prior art date
1979-11-09
Legal status (The legal status 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 status listed.)

Abandoned

Application number
AU65768/80A
Inventor
John J. Allport
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

ZIKONIX CORP

Original Assignee
ZIKONIX CORP
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.)
1979-11-09
Filing date
1980-11-05
Publication date
1981-06-03

1979-11-09
Priority claimed from US06/092,983
external-priority
patent/US4266425A/en

1980-11-05
Application filed by ZIKONIX CORP
filed
Critical
ZIKONIX CORP

1981-06-03
Publication of AU6576880A
publication
Critical
patent/AU6576880A/en

Status
Abandoned
legal-status
Critical
Current

Links

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Global Dossier

Discuss

Description

– 1 –
Description
Method For Continuously Determining The Composition And Mass Flow Of A Slurry
Technical Field This invention relates to the measurement of the instantaneous composition and mass flow of a- slurry such as butter, margarine, peanut butter, cream cheese and similar substances.
Background Art In the production of butter by machines, the fat and moisture content of the product must be closely regulated. Moisture gauges have been built previously to directly sense moisture in butter, but the gauges are far from accurate. The moisture usually has been sensed capacitively, using radio frequency sensors. However, the dielectric constant, which determines capacitance, varied not only with moisture, but also with density, a parameter not measured or detected by the prior moisture gauges. Density varies in butter because of different amounts of air introduced by the churning process. Although some butter machines employ vacuum sections to remove the air, the density varia¬ tion still is large enough to render the dielectric constant measurement commercially useless as an indi- cator of moisture content.
Gamma-ray and X-ray gauges have been developed for determining material density by measuring the transmis¬ sion of radiation through the material. The ratio (R) of radiation transmitted through the material (I.) to

that detected in the absence of the material (I ) may be written:

where u is the apparent mass absorption coefficient, p is the unknown density and T is the thickness of the material. In a closed pipe, completely filled with the material, I_. and I can be measured with radia¬ tion detectors, and since the thickness T is known the density may be determined on a continuous basis.
The composition of simple, essentially binary, mixtures have be:en shown to be measurable in the prior art using backscattered X-ray or gamma-ray radiation. (See for example: U.S. Patent No. 4,168,431, and 3,255,975) – »
In another invention, owned by the assignee of this invention, E. Dahlin has shown’ how a feedback control system using butter density and moisture content control signals, can be used as important parameters in operating a butter machine. While a static density and moisture control signals could be generated, for example by laboratory measurement, dynamic signals are preferable. By «dynamic signal» is meant a continuous real time or instantaneous measurement, as the butter is produced.
The need for a dynamic composition measurement signal exists not only in butter production, but in many industrial process applications, where the com¬ position of the end product is slightly variable and knowledge of the variations is important.
In the same previously mentioned invention by E. Dahlin, a need is shown for measurement of the mass flow of butter from a butter machine. While average mass may be determined by weighing the product pro¬ duced over a period of time, it is better to have a
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continuous measurement represented by a dynamic sig¬ nal. A mass flow determination from a butter machine requires a real time density measurement, together with a measure of the butter flow velocity at a known dimensional cross section.
Disclosure of Invention
An object of the invention is to accurately measure the instantaneous composition, namely moisture and fat content, as well as the instantaneous mass flow of butter and salt content to provide signals for use in generating control signals for butter production.
The above object has been met with a non¬ destructive method for determining the compositional content of a slurry. In the case of butter and similar substance, fat and water content are measured.
The method of this invention relies on contin¬ uously measuring the density of the substance as it emerges from the manufacturing process. A simultaneous continuous measurement is made of either the dielectric constant or the radiation backscatter intensity.
Either one of the latter measurements provides infor¬ mation which can be combined with density information for a determination of substance composition.
In the case of a salted substance brine flow into the manufacturing process is also measured. A measure¬ ment of the butter mass flow is also needed in order to convert the brine flow information into a salt content determination. Mass flow is continuously determined by measuring the velocity of the substance out of the process and combining the density measurement with the velocity measurement.
All of the measured information is gathered non-destructively and fed to a computer. The computer

has a memory wherein calibration data from prior tests is stored. By comparing the calibration data with the measured dielectric constant or backscatter intensity, the measured density, the known curd content, the velocity, and in the case of a salted substance the brine flow, composition and mass flow of the substance may be calculated. Specifically, water, fat, mass flow, and in the case of a salted substance, the salt content are calculated for process control purposes.
Brief Description of Drawings
Figure 1 is a plan view of a measurement system for continuously determining the composition and mass flow of butter from a butter machine in accord with the present invention. Figure 2 is a plan view of an alternate measure¬ ment system for continuously determining the composi¬ tion and mass flow of butter from a butter machine in accord with the present invention.
Best Mode for Carrying Out the Invention With reference to* Figure 1 , the output of a butter machine is schematically depicted by arrows A. Such a machine has a silo which feeds cream into the machine where blades churn the cream causing formation of large butter globules after a time. These globules are car- ried into a separator section where a device such as a screen or a centifugal rotor causes separation of the butter and further agglomeration from the butter¬ milk. Water and brine may be added through a pipe by a control valve to provide the desired moisture content to the butter which is advanced by an auger.
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An auger compresses the butter and works it into a mass which is extruded from a duct 11. This explana¬ tion of a butter machine is greatly simplified. Many machines include auxiliary features, such as a vacuum section and other blending sections. From the duct 11, a column of butter B emerges which is advanced in the direction of the arrow A by continuous motion of the auger.
In accord with the present invention, the auger provides the power for continuously advancing a column of butter B through a duct having a constant dimen¬ sional cross section containing a measuring section which is positioned near the machine outlet. The dimensions of the duct 11 determine the cross section of the butter column.
The measuring station consists of a radio isotope density sensor 13, a capacit’ive moisture sensor 15 and a velocimeter 17. Each of these sensors produces an electrical output signal which is electrically connected to a digital computer 19 having an auxiliary memory. This connection is achieved through a computer interface 21 which serves to convert analog signals to a digital format and to multiplex the signals. In accord with the present invention the memory of com- puter 19 is loaded with calibration information regard¬ ing the measured densities of butter for various known fat and moisture contents which can be made using the butter machine. Different densities can be achieved by operating the machine with different beater speeds, auger speeds, as well as by applying different doses of moisture or brine. Other differences in density arise from differences in the composition of the cream used or because of different amounts of air entrained in the production process.

The density of the butter is measured by the density sensor 13. This sensor is of a known transmis- sive X-ray or radioisotope type. A radioactive source, such as Americium 241 is housed in canister 23. Such a source emits gamma rays with a principal energy peak at 59.7kev. A detector 25 is positioned on the opposite side of butter column B so that the gamma rays passing through the aperture of detector 43 have passed through the butter column B. The detector 43 is of the type which produces an electrical signal proportional to the intensity (I..) of gamma rays which are detected. This electrical signal is transmitted along line 27 to the computer interface 21. Prior to reading the gamma ray intensity through the butter, an intensity signal (I ) is measured in the absence of butter. The computer 19 then computes the ratio R of the intensities in accord with equation ( 1 ) . Since the transverse dimension of the sample is known from the dimensions of the duct 11 and since at 59.7kev the apparent mass absorption coefficient for butter is known and is not essentially composition dependent, the unknown density may be calculated from equation (1). This calculation is made in computer 19. The computer is able to compute density as fast as radiation intensity signals are received and so the computer is able to produce a dynamic signal representing the instantaneous density of butter as it emerges from the butter machine.
If the density is known, moisture content may be measured either by means of radio frequency techniques which sense the dielectric constant of the butter, or alternatively the composition may be determined by measuring the intensity of backscattered X-ray or gamma-ray radiation at a properly chosen energy as will be seen below.
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At the same time that density is being measured, the instantaneous dielectric constant of the butter column is also being measured by the sensor 15. This is a capaciriive sensor which measures dielectric con- stant in the radio frequency spectrum. Such devices are known in prior art and one such dielectric constant sensor is manufactured by Brabender Messteσhnik of Duisburg, W.Germany. An explanation of this type of dielectric constant sensor is contained in the article «Kontinuierliche Wassergehalts essung an Butter» by
W. Heinz. Preferred radio frequencies are in the range from 1MHz to 100 MHz. Microwave propagation and reflection techniques may also be employed. They introduce more complexity however, with no increase in accuracy. This gives a dynamic signal transmitted along line 29, with signal strength or intensity functionally dependent on the dielectric constant of the butter. In turn, the dielectric constant is proportional to moisture content and density in accord with known relationships. For example. Table 1 in the above mentioned article shows that when the percentage of water in butter varies from 0 to 30% the correspond¬ ing measured dielectric constant ranges from 3.2 to 11.6. Thus, the measured dielectric constant must be corrected by the measured density value to obtain a value that is proportional to moisture. This correc¬ tion may be done by a computer. The memory of the computer contains information indicating how the dielectric constant of the butter varies with composi- tion and density. Once the measured dielectric con¬ stant and measured density as well as the known curd content signals are fed into the computer, the com¬ position (water and fat content) may be calculated. The finished butter moves as a mass through the duct 11 of known cross section from the machine. The

velocity may therefore be measured by acoustical or optical doppler shift measurements or by means of a wheel 31 which is turned by butter motion which in turn drives a rotary encoder 33. A velocity signal is transmitted to the computer along line 34. Once the velocity is known and the instantaneous density is known, the mass flow can be computed in the usual manner using the known duct cross section.
In the event that brine is introduced from a supply 35 into the butter machine through a valve 37 so that salted butter is produced, the flow rate of the brine is measured at a valve introducing the brine into the manufacturing process and a signal representing this flow rate is transmitted along line 39 to the computer 19 via interface 21. Since the brine has a known salt content, the flow rate, together with the mass flow rate of butter, indicates the amount of salt being introduced into the butter. This informa¬ tion is useful since the salt content also affects the dielectric constant measurement. Alternatively the salt in the slurry may be measured directly by sensing the backscattered soft gamma ray radiation of the slurry, by the salt sensor 18. Salt sensor 18 com¬ prises a soft gamma ray source 60 and a detector 62 to measure the amount of backscattered radiation.
The memory of the computer also contains information indicating the manner in which the dielectric constant of the butter varies with salt content. Once the salt content signal is fed to the computer together with the dielectric constant, the density, and the known curd content the composition (water and fat content) may be calculated continuously. The same is done when no brine signal is present.
Computer 19 also receives data from a laboratory 41 where the cream and butter are periodically tested
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for curd content. The curd content of the butter produced in a given machine has been found to correlate directly with the curd content in cream and the fat content in the butter. Before the machine is started the curd content of the cream in the silo is measured and used to determine the curd content expected in the butter. This value of curd content is entered into the computer as an initial value. Once the butter production has started a sample of the butter is taken and quickly analyzed in the laboratory for curd con¬ tent, this value is then entered into the computer and used as the known curd content for the rest of the production run. Similarly, the salt content of the brine is measured and remains unchanged.in the manu- facturing process. Signals representing this data are transmitted from laboratory 41 to computer 19 on a periodic basis, as needed.
The computer is able to compute the fat, moisture and salt content by comparing the measured values of the parameters mentioned above, such as density, dielectric constant, mass flow, brine flow and curd content with data from calibration trials where each of the parameters was measured in the laboratory by tests. The test data is stored in the computer for different runs of the butter machine representing the conditions under which the machine is expected to operate.
The output of the computer 19 includes butterfat content taken along line 43, the water content on line 45, the salt content, if any, on line 47, the curd content on line 49 and the mass flow on line 51. These outputs are transmitted to a control panel 53 for a butter machine where the data may be viewed, recorded and used to control process operation.
Figure 2 illustrates an alternate means of measur- ing the corrected density of the butter. The system is

the same as in Figure 1 except that the dielectric constant sensor 15 is replaced by a backscatter sensor 16. A radioactive source is housed in a canister 24 similar to the source housed in canister 23. Low energies provide the best discrimination, however they also represent instrumental problems. In the case of butter a good choice is X-ray or gamma-ray radiation in the approximate energy range 15 to 25kev. The density is best measured using X-ray or gamma-ray radiation of higher energy such that it is not affected byj the composition variances which may occur. For butter, one chooses energies in excess of 45kev. A radiation detector is housed in the canister 26, simi¬ lar to the canister 25. The detector in canister 26 is positioned for measuring radiation backscattered from the butter column. The backscatter intensity is inversely proportional to the photoelectric cross section of the butter. It is well known that water molecules have a higher photo-electric cross section than fat molecules. Accordingly, intensity of back- scattered radiation decreases as the percentage of water increases. A signal proportional to the back- . scattered intensity is taken along line 30 and trans¬ mitted to the computer. The radiation source might be an Americium 241 source with a Beryllium window which permits emission of the Neptunium L X-rays of average energy about 17.7kev which are nearly ideal in energy for determining the composition of butter. The detector housed in canister 26 is optimized for detect- ing the Neptunium L X-rays and is made insensitive to the 59.7kev Americium 241 gamma rays. The measured density is used to provide minor corrections, as required, to the composition as determined from the backscattered energy at 17.7kev.
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When salted butter is produced, the backscattered intensity depends on the salt content as well as the water and fat content because the photoelectric absorp¬ tion cross sections of sodium and chlroine are con- siderably larger than those of butterfat and water at the low energies employed. The measured brine flow rate and the measured butter mass flow rate are deter¬ mined however, as described earlier, and are used to determine the salt content of the butter. The deter- mined salt content, the known curd content, together with the density, and the backscattered intensity, along with calibration data stored in the computer are then used to determine the butter composition, namely water and fat content as previously described. While this invention has been described with reference to butter production, the same system may be applied to the production of margarine and to liquid dairy products, as well as other essentially binary or tertiary products.

Claims (12)

Claims

1. A non-destructive method for continously and instantaneously determining the compositional content of a slurry moving in a stream, wherein said slurry is a mixture of at least two substances, at least one of which is a liquid, said method comprising: continuously measuring one parameter of the slurry to obtain a first value; continuously measuring another parameter of the slurry to obtain a second value; continuously comparing said first and second values to a set of known first and second values; and continuously calculating the composi¬ tional content of the slurry based upon said comparison

2. A non-destructive method for continuously and instantaneously determining the compositional content of a slurry moving in a stream, wherein said slurry is a mixture of at least two substances, at least one of which is a liquid, said method comprising: continuously measuring one parameter of – the slurry- to obtain a first value that is primarily dependent upon the density of the slurry; continuously measuring another parameter of said slurry to obtain a second value that is primarily dependent upon the liquid content of the slurry; continuously correcting the second value by the first value; and continuously calculating the composi¬ tional content of the slurry based upon the corrected second value and the first value.
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3. The method of Claim 1 or 2 further comprising: continuously measuring the velocity of the slurry moving in said stream; and continuously calculating the mass flow of said slurry.

4. The method of Claim 3 wherein said liquid is water.

5. The method of Claim 4 wherein said slurry has a known curd content and said compositional content is fat and water.

6. The method of Claim 5 further comprising continuously measuring the salt content of said slurry.

7. The method of Claim 6 wherein said composi¬ tional content of the slurry further includes salt.’

8. The method of Claim 7 wherein said slurry is butter.

9. The method of Claim 8 wherein said measuring steps are performed immediately after the butter emerges from the manufacturing process.

10. The method of Claim 9 wherein said measuring one parameter step is accomplished by the use of transmissive x-rays or gamma rays.

11. The method of Claim 10 wherein said measuring another parameter step is accomplished by the use of low energy backscattered x-rays or gamma rays.

12. The method of Claim 10 wherein said measuring another parameter step is accomplished by the use of radio frequencies.
OMPI

AU65768/80A
1979-11-09
1980-11-05
Method for continuously determining the composition and mass flow of a slurry

Abandoned

AU6576880A
(en)

Applications Claiming Priority (3)

Application Number
Priority Date
Filing Date
Title

US092,983

1979-11-09

US06/092,983

US4266425A
(en)

1979-11-09
1979-11-09
Method for continuously determining the composition and mass flow of butter and similar substances from a manufacturing process

PCT/US1980/001482

WO1981001468A1
(en)

1979-11-09
1980-11-05
Method for continuously determining the composition and mass flow of a slurry

Publications (1)

Publication Number
Publication Date

AU6576880A
true

AU6576880A
(en)

1981-06-03

Family
ID=26762850
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

AU65768/80A
Abandoned

AU6576880A
(en)

1979-11-09
1980-11-05
Method for continuously determining the composition and mass flow of a slurry

Country Status (2)

Country
Link

AU
(1)

AU6576880A
(en)

DE
(1)

DE3050031A1
(en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

DE19613234A1
(en)

1996-04-02
1997-10-09
Funke Dr N Gerber Gmbh
Simplified thermal conductivity cell determining fat content of milk accurately

1980

1980-11-05
DE
DE19803050031
patent/DE3050031A1/en
not_active
Withdrawn

1980-11-05
AU
AU65768/80A
patent/AU6576880A/en
not_active
Abandoned

Also Published As

Publication number
Publication date

DE3050031A1
(en)

1982-06-03

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