US3186596A - Concrete batch blending control system - Google Patents
Concrete batch blending control system Download PDFInfo
- Publication number
- US3186596A US3186596A US168689A US16868962A US3186596A US 3186596 A US3186596 A US 3186596A US 168689 A US168689 A US 168689A US 16868962 A US16868962 A US 16868962A US 3186596 A US3186596 A US 3186596A
- Authority
- US
- United States
- Prior art keywords
- ingredient
- measuring section
- mass flow
- blender
- chute
- Prior art date
- 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.)
- Expired - Lifetime
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C7/00—Controlling the operation of apparatus for producing mixtures of clay or cement with other substances; Supplying or proportioning the ingredients for mixing clay or cement with other substances; Discharging the mixture
- B28C7/04—Supplying or proportioning the ingredients
- B28C7/0404—Proportioning
- B28C7/0409—Proportioning taking regard of the moisture content of the solid ingredients; Moisture indicators
Definitions
- This invention relates generally to cement blending processes and more particularly to a system for measuring and controlling a batch concrete blender.
- the present invention provides means for performing a non-contacting measurement of mass flow of the material as it falls by gravity from the supply or feed bin into the blender.
- the amount of moisture is determined and the two measurements are used to compute the mass flow of dry material and water.
- the mass flow measurements are integrated over a period of time to drive a signal proportional to total mass. The fiow is cut off when sulficient time has elapsed for a desired total mass to be transferred to the blender.
- FIG. 1 is a block diagram of a measuring and controlling system for a batch concrete blending process constructed in accordance with the present invention.
- FIG. 2 is a diagrammatic view of a controller for use in the system shown in FIG. 1.
- the system of the present invention is embodied in a batch concrete blending process including a storage bin 10 for feeding or supplying either aggregate, sand or cement.
- a pair of swingable metering gates 12 serve to admit the material contained in the bin 10 to a chute 14.
- the material falls by gravity down the chute 14 into a blender 16 which may comprise a mixing truck used to transport concrete to the construction site.
- the mass flow M of material into the blender 16 is a function of the bulk density p of the material, the crosssectional area A of the stream of material and the velocity v.
- a radiation density gauge is provided by a source of gamma radiation 26) and a detector 22 therefor mounted on opposite sides of the chute 14.
- the detector may comprise one or more Geiger-Muller tubes responsive to radiation passing through the chute and falling material.
- An amplifier 24 provides a signal M which is a function of the total mass of material intercepting the gamma radiation beam passing from the source 20 to the detector 22.
- the radiation beam passes through substantially the total cross-sectional area A of the chute, even though the actual cross-sectional area A of the material stream is generally less than A and dependent on the selected width of the opening provided by the metering gates 12 in their open position.
- Equation 1 may thus be replaced by the equivalent expression Particularly if the source 20 and detector 22 are placed as close as possible to the metering gates 12 as shown, the free fall velocity is also substantially constant, and hence the signal M varies essentially only with and is in fact an accurate indication of the mass flow M.
- the total mass flow signal M include a component due to the moisture entrained in the material.
- a source 26 of neutron radiation and a detector 28 are mounted near to the gamma ray source and detector units 2! 22 and connected to an amplifier 30.
- a signal M proportional to the moisture mass flow is provided by amplifier 30 on line 32.
- a computer 34 provides a signal M proportional to the mass flow of the dry material alone and transmits it to a chart recorder 36.
- the chart recorder presents a continuous trace 38 on a moving chart 40.
- the chart trace 38 may be interpreted as mass flow vs. time as indicated by the coordinate axes to the right.
- the left-hand line or trace portion 38a is indicative of the empty chute while the displaced curvilinear portion 38b represents measurements of the falling material.
- the time of fall At is indicated and may typically extend for 20 to 40 seconds.
- the dry mass flow signal M is also transmitted to an integrator 42 which in turn provides a signal proportional to the total dry mass transferred to the blender.
- This signal is represented as dt where T2T1:At
- a remote unit 44 may be used to enable dispatching personnel to dial in a preferred value for m.
- the selected value for m is converted by unit 44 to a constant analog signal that is delivered to an error sensing unit 46.
- Unit 46 compares this signal with the output signal from integrator 42 and provides an error signal proportional to the difference therebetween. When the integrator output signal becomes equal to the signal representing the selected value for m, the error signal is reduced to zero.
- Controller 48 responds to the condition of zero output from the error sensor 46 to operate an air cylinder 54 adapted to actuate the metering gates 12.
- the controller 48 described in detail hereinafter basically determines how long the gates 12 remain open by closing the gates when the proper amount of material has been transferred to the blender. If a large mass flow M is measured, the gates are not open for nearly the duration as if a smaller mass fiow were being measured.
- Another controller 52 servesto control the amount of water added to the blender from a supply 54.
- a servomotor 56 is mechanicallylinked as indicated by the dotted line 58 to a valve 60 connecting the water supply 54 to the blender 16.
- the controller 52 may include suitable integrating, error sensing and set point adjusting units similar to those described above. The controller operates the servomotor 56 in such a direction as to keep the entrained moisture and added moisture to the blender at a preferred value consistent with good operating practice.
- the controller 48 may include a timer 62 operative to apply electrical power from a supply 64 to a solenoid 66 mechanically coupled to the metering gates 12.
- the timer is usually required to shorten or lengthen the variable integration period At by a fixed amount which depends on either or both the time required for the material to fall from the gates 12to the source detector or the time required to compensate for an inherent mechanical delay in the closing of the gates.
- the timer may be influenced by the error signal to shorten or prolong the period of operation of the sole- 7 noid 66.
- the timer 62 may comprise a thyratron whose period of cutoff is determined by the bias caused by the error signal leaking oii of an R-C network. Other timing expedients of equal utility may be suggested.
- Batch concrete blending apparatus which comprises: a storage bin for a nominally dry ingredient having an unknown moisture content, a blender, a chute leading directly from said bin to said blender and having a measuring section provided in said 7 chute,
- gate means located between said bin and said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender;
- said gate, said chute and said measuring section therein being arranged so that said ingredient passes through said measuring section at a relatively constant velocity
- Batch concrete blending apparatus which comprises: a storage bin for a nominally dry ingredient having an unknown moisture content,
- gate means located between said bin and said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender;
- said gate, said chute and said measuring section therein a it being arranged so that said ingredient passes through said measuring section at a relatively constant velocmeans responsive to the apparent, bulk density of material in said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
- said water "delivery means in accordance with the amount of moisture entrained in said nominally dry ingredient.
- Batch concrete blending apparatus which comprises:
- target setting means for providing a target signal indicative of a desired massof said ingredient in said dry state
- I k a controller including timer means having a time setting biased by a combination of said integral and target signals for initiatingclosureof said gate when said desired mass of said-ingredient plus the moisture entrained therein has passed through said gate.
- Batch concrete blending apparatus which comprises a storage bin for a nominally dry ingredient having an unknown moisture content, r
- target setting means for providing a target signal in dicative of a desired mass of said ingredient in said dry state
- a controller including timer means having a time setting biased by a combination of said integral and target signals for initiating closure of said gate when said desired mass of said ingredient plus the moisture entrained therein has passed through said gate,
- adjustable means for delivering water to said blender for combination with said ingredient therein
- Batch concrete blending apparatus which comprises:
- gate means located at the top of said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender after falling at a substantially constant velocity through said measuring section
- means including a detector for said gamma rays mounted on the opposite side of said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
- Batch concrete blending apparatus which comprises:
- gate means located at the top of said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender after falling at a substantially constant velocity through said measuring section
- means including a radiation detector mounted on the opposite side of said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
- means including a second radiation detector on the other side of said measuring section opposite said neutron source for providing a signal indicating the rate of moisture mass fiow accompanying the fiow of said ingredient therethrough,
Description
June 1, 1965 c. o. BADGETT 3,186,596
CONCRETE BATCH BLENDING CONTROL SYSTEM Filed Jan. 25, 1962 SAND AGGREGATE c MENT r l I REMOTE TARGET 2 lo I SETTER f e ERROR CONTROLLER SENSING 50 I: l2 INTEGRATOR 42 v T K l I I l l I I l l l l I I4 -\58 38 I WATER F6) SUPPLY M BLENDER 380 METERING L- GATES TIMER Inventor ATTORN EY United States Patent 3,1865% 7 CUNQRETE BATCH BLENBTNG CONTRGL SYSTEM Charles '9. Eadgett, Qolunrhus, Uhio, assignor to Industrial Nucleonics Qorporatinn, a corporation of @hio Filed lap. 25, 1%2, Ser. No. 163,689 6 Qlairns. (Cl. ZZZ-14) This invention relates generally to cement blending processes and more particularly to a system for measuring and controlling a batch concrete blender.
In batch concrete blending, dry aggregate, sand, and cement materials are individually weighed and admitted to a blender Where water is added to provide concrete having a certain desired consistency and preferred strength characteristics. The weigh hoppers commonly used are only as accurate as good maintenance of the knife edges will permit. These mechanical weighers malfunction due to cement and dust deposits which build up and must be removed. The weigh hoppers must be placed below the feed bins and expensive supporting structure is required to provide clearance below the weigh hoppers for trucks or other blending equipment.
In addition, there is always present a certain indeterminate amount of moisture present in these materials admitted to the feed bins. The amount of entrained water varies with the weather and other environmental factors which are usually uncontrollable. As a result the concrete produced may be entirely too wet. In the manufacture of building block this could result in blocks of inferior strength due to the inability of the equipment to cope with the overdampened mix.
The present invention provides means for performing a non-contacting measurement of mass flow of the material as it falls by gravity from the supply or feed bin into the blender. The amount of moisture is determined and the two measurements are used to compute the mass flow of dry material and water. The mass flow measurements are integrated over a period of time to drive a signal proportional to total mass. The fiow is cut off when sulficient time has elapsed for a desired total mass to be transferred to the blender.
Accordingly, it is a primary object of the present invention to provide an improved measuring and control system for a batch concrete blending process.
It is another object of the present invention to provide a system which is more accurate and more reliable than similar devices used heretofore.
It is still another object of the present invention to provide a system which is completely automatic and capable of increased throughput.
It is yet another object of the present invention to provide a system which requires less space and fewer supporting structures than similar devices used heretofore.
These and other objects and features of the present invention will become more apparent when the following description is taken in conjunction with the attached drawings, in which:
FIG. 1 is a block diagram of a measuring and controlling system for a batch concrete blending process constructed in accordance with the present invention; and
FIG. 2 is a diagrammatic view of a controller for use in the system shown in FIG. 1.
With reference now to the drawings and specifically to FIG. 1, the system of the present invention is embodied in a batch concrete blending process including a storage bin 10 for feeding or supplying either aggregate, sand or cement. A pair of swingable metering gates 12 serve to admit the material contained in the bin 10 to a chute 14. The material falls by gravity down the chute 14 into a blender 16 which may comprise a mixing truck used to transport concrete to the construction site.
r M= 'Av, wherein A is constant.
3,l35,596 Patented June 1, 1965 The mass flow M of material into the blender 16 is a function of the bulk density p of the material, the crosssectional area A of the stream of material and the velocity v. Mathematically,
M=pAv (1) In accordance with the invention a radiation density gauge is provided by a source of gamma radiation 26) and a detector 22 therefor mounted on opposite sides of the chute 14. The detector may comprise one or more Geiger-Muller tubes responsive to radiation passing through the chute and falling material. An amplifier 24 provides a signal M which is a function of the total mass of material intercepting the gamma radiation beam passing from the source 20 to the detector 22. The radiation beam passes through substantially the total cross-sectional area A of the chute, even though the actual cross-sectional area A of the material stream is generally less than A and dependent on the selected width of the opening provided by the metering gates 12 in their open position. Hence the signal M, is a function of an apparent bulk density proportional to the mass per unit volume of the measured region of the chute including air spaces therein. Equation 1 may thus be replaced by the equivalent expression Particularly if the source 20 and detector 22 are placed as close as possible to the metering gates 12 as shown, the free fall velocity is also substantially constant, and hence the signal M varies essentially only with and is in fact an accurate indication of the mass flow M.
It is inevitable that the total mass flow signal M include a component due to the moisture entrained in the material. To measure this component a source 26 of neutron radiation and a detector 28 are mounted near to the gamma ray source and detector units 2! 22 and connected to an amplifier 30. A signal M proportional to the moisture mass flow is provided by amplifier 30 on line 32.
A computer 34 provides a signal M proportional to the mass flow of the dry material alone and transmits it to a chart recorder 36. The chart recorder presents a continuous trace 38 on a moving chart 40. The chart trace 38 may be interpreted as mass flow vs. time as indicated by the coordinate axes to the right. The left-hand line or trace portion 38a is indicative of the empty chute while the displaced curvilinear portion 38b represents measurements of the falling material. The time of fall At is indicated and may typically extend for 20 to 40 seconds.
The dry mass flow signal M is also transmitted to an integrator 42 which in turn provides a signal proportional to the total dry mass transferred to the blender. This signal is represented as dt where T2T1:At A remote unit 44 may be used to enable dispatching personnel to dial in a preferred value for m. The selected value for m is converted by unit 44 to a constant analog signal that is delivered to an error sensing unit 46. Unit 46 compares this signal with the output signal from integrator 42 and provides an error signal proportional to the difference therebetween. When the integrator output signal becomes equal to the signal representing the selected value for m, the error signal is reduced to zero. Controller 48 responds to the condition of zero output from the error sensor 46 to operate an air cylinder 54 adapted to actuate the metering gates 12. The controller 48 described in detail hereinafter basically determines how long the gates 12 remain open by closing the gates when the proper amount of material has been transferred to the blender. If a large mass flow M is measured, the gates are not open for nearly the duration as if a smaller mass fiow were being measured.
Another controller 52 servesto control the amount of water added to the blender from a supply 54. A servomotor 56 is mechanicallylinked as indicated by the dotted line 58 to a valve 60 connecting the water supply 54 to the blender 16.. The controller 52 may include suitable integrating, error sensing and set point adjusting units similar to those described above. The controller operates the servomotor 56 in such a direction as to keep the entrained moisture and added moisture to the blender at a preferred value consistent with good operating practice.
Referring to FIG. 2, the controller 48 may include a timer 62 operative to apply electrical power from a supply 64 to a solenoid 66 mechanically coupled to the metering gates 12.. The timer is usually required to shorten or lengthen the variable integration period At by a fixed amount which depends on either or both the time required for the material to fall from the gates 12to the source detector or the time required to compensate for an inherent mechanical delay in the closing of the gates. Briefly, the timer may be influenced by the error signal to shorten or prolong the period of operation of the sole- 7 noid 66. The timer 62may comprise a thyratron whose period of cutoff is determined by the bias caused by the error signal leaking oii of an R-C network. Other timing expedients of equal utility may be suggested.
While certain and specific embodiments have been described herein, many changes and modifications may be made without departing from the true spirit and scope of the invention as is set forth in the appended claims.
I claim: 1. Batch concrete blending apparatus which comprises: a storage bin for a nominally dry ingredient having an unknown moisture content, a blender, a chute leading directly from said bin to said blender and having a measuring section provided in said 7 chute,
gate means located between said bin and said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender;
said gate, said chute and said measuring section therein being arranged so that said ingredient passes through said measuring section at a relatively constant velocity;
means responsive to the apparent bulk density of material in said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
means responsive to the moisture contained in material in said measuring section for providing a signal indicating the rate of moisture mass flow accompanying the flow of said nominally dry ingredient therethrough,
computer means for mathematically combining said moisture mass flow signal with said ingredient mass flow signal to provide a compensated mass flow signal indicating the mass flow of said ingredient in a dry state,
means for computing a time integral of said compensated mass flow signal, and
'means for closing said gate when said computed in tegral exceeds a predetermined value,
2. Batch concrete blending apparatus which comprises: a storage bin for a nominally dry ingredient having an unknown moisture content,
a blender,
a chute leading directly from said bin to said blender and having a measuring section provided in said chute,
gate means located between said bin and said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender;
said gate, said chute and said measuring section therein a it being arranged so that said ingredient passes through said measuring section at a relatively constant velocmeans responsive to the apparent, bulk density of material in said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
means responsive to the moisture contained in material in said measuring section for providing a signal indicating the rate of moisture mass flow accompanying the flow of said ingredient therethrough,
computer means for. mathematically combining said moisture mass flow signal with said ingredient mass flow signal to provide a compensated mass flow signal indicating the mass flow of said ingredient in a dry state,
means for computing a time integral or said compensated mass flow signal,
means for closing said gate when said computed integral exceeds a predetermined value,
adjutsable means'for delivering water to said blender for combination with said ingredient therein, and
means responsive to a function of saidmoisture mass flow signal for adjusting. said water "delivery means in accordance with the amount of moisture entrained in said nominally dry ingredient.
3. Batch concrete blending apparatus which comprises:
a storage bin for a nominally dry ingredient having an unknown moisture content,
a blender,
a chute leading directly from said bin to said blender and having a vertical measuring section provided in said chute wherethrough said ingredient can fall freely under the influence of gravity,
gate means located at thetop of said measuring section for admitting said ingredient thereto whereby said ingredient passes to said blender after falling at a substantially constant velocity through said measuring section, V
means responsive to the apparent bulk density of material in said measuringjsection for vproviding a signal indicating the rate of mass flow of said ingredient therethrough,
means responsive to the moisturecontained in material in said measuring section for providing a signal indicating the rate of moisture mass flow accompanying the flow of said ingredient therethrough,
computer means for mathematically combining said moisture mass flowsignalwith said ingredient mass fiowsignal to provide a compensated mass flow signal indicating the mass flow of said ingredient in a dry state,
means for computing a time integral or said cornpensated mass flow signal,
target setting means for providing a target signal indicative of a desired massof said ingredient in said dry state, and I k a controller including timer means having a time setting biased by a combination of said integral and target signals for initiatingclosureof said gate when said desired mass of said-ingredient plus the moisture entrained therein has passed through said gate.
4. Batch concrete blending apparatus which comprises a storage bin for a nominally dry ingredient having an unknown moisture content, r
a blender,
a chute leading directly from said bin to. said blender and having a vertical measuring section provided insaid chute wherethrough said ingredient can fall freely'under the influence of gravity,
gate means located at the top of said measuring sec- 7 tion for admitting said ingredient thereto whereby said ingredient passes to said blender after falling at a substantially constant velocity through said measuring section,
means responsive to the apparent bulk density of material in said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
means responsive to the moisture contained in mate rial in said measuring section for providing a signal indicating the rate of moisture mass flow accompanying the flow of said ingredient therethrough,
computer means for mathematically combining said moisture mass flow signal with said ingredient mass flow signal to provide a compensated mass flow signal indicating the mass flow of said ingredient in a dry state,
means for computing a time integral of said compensated mass flow signal,
target setting means for providing a target signal in dicative of a desired mass of said ingredient in said dry state,
a controller including timer means having a time setting biased by a combination of said integral and target signals for initiating closure of said gate when said desired mass of said ingredient plus the moisture entrained therein has passed through said gate,
adjustable means for delivering water to said blender for combination with said ingredient therein, and
means responsive to a function of said moisture mass flow signal for adjusting said water delivery means in accordance with the amount of moisture entrained in said nominally dry ingredient.
5. Batch concrete blending apparatus which comprises:
a storage bin for a nominally dry ingredient,
a blender,
a chute leading directly from said bin to said blender and having a vertical measuring section provided in said chute wherethrough said ingredient can fall freely under the influence of gravity,
gate means located at the top of said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender after falling at a substantially constant velocity through said measuring section,
a source of gamma rays mounted on one side of said measuring section,
means including a detector for said gamma rays mounted on the opposite side of said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
means for computing a time integral of said signal,
and
means for closing said gate when said computed integral exceeds a predetermined value.
6. Batch concrete blending apparatus which comprises:
a storage bin for a nominally dry ingredient having an unknown moisture content,
a blender,
a chute leading directly from said bin to said blender and having a vertical measuring section provided in said chute wherethrough said ingredient can fall freely under the influence of gravity,
gate means located at the top of said measuring section for admitting said ingredient to said chute whereby said ingredient passes to said blender after falling at a substantially constant velocity through said measuring section,
a source of gamma rays mounted on one side of said measuring section,
means including a radiation detector mounted on the opposite side of said measuring section for providing a signal indicating the rate of mass flow of said ingredient therethrough,
a source of neutron radiation mounted on one side of said measuring section,
means including a second radiation detector on the other side of said measuring section opposite said neutron source for providing a signal indicating the rate of moisture mass fiow accompanying the fiow of said ingredient therethrough,
computer means for mathematically combining said moisture mass flow signal with said ingredient mass flow signal to provide a compensated mass flow signal indicating the mass flow of said ingredient in a dry state,
means for computing a time integral of said compensated mass flow signal, and
means for closing said gate when said computed integral exceeds a predetermined value.
References (Jited by the Examiner UNITED STATES PATENTS 2,510,158 6/50 Van Ackeren 222-57 X 2,710,715 6/55 Gorham 141-130 2,864,537 12/58 Throop et a1 222-67 2,880,764 4/59 Pelavin 14l130 2,909,303 10/59 Henderson et al 22257 RAPHAEL M. LUPO, Primary Examiner. LAVERNE GE IGER, HADI? LANE, Examiners,
Claims (1)
1. BATCH CONCRETE BLENDING APPARATUS WHICH COMPRISES: A STORAGE BIN FOR A NOMINALLY DRY INGREDIENT HAVING AN UNKNOWN MOISTURE CONTENT, A BLENDER, A CHUTE LEADING DIRECTLY FROM SAID BIN TO SAID BLENDER AND HAVING A MEASURING SECTION PROVIDED IN SAID CHUTE, GATE MEANS LOCATED BETWEEN SAID BIN AND SAID MEASURING SECTION FOR ADMITTING SAID INGREDIENT TO SAID CHUTE WHEREBY SAID INGREDIENT PASSES TO SAID BLENDER; SAID GATE, SAID CHUTE AND SAID MEASURING SECTION THEREIN BEING ARRANGED SO THAT SAID INGREDIENT PASSES THROUGH SAID MEASURING SECTION AT A RELATIVELY CONSTANT VELOCITY; MEANS RESPONSE TO THE APPARENT BULK DENSITY OF MATERIAL IN SAID MEASURING SECTION FOR PROVIDING A SIGNAL INDICATING THE RATE OF MASS FLOW OF SAID INGREDIENT THERETHROUGH, MEANS RESPONSIVE TO THE MOISTURE CONTAINED IN MATERIAL IN SAID MEASURING SECTION FOR PROVIDING A SIGNAL INDICATING THE RATE OF MOISTURE MASS FLOW ACCOMPANYING THE FLOW OF SAID NOMINALLY DRY INGREDIENT THERETHROUGH,
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US168689A US3186596A (en) | 1962-01-25 | 1962-01-25 | Concrete batch blending control system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US168689A US3186596A (en) | 1962-01-25 | 1962-01-25 | Concrete batch blending control system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3186596A true US3186596A (en) | 1965-06-01 |
Family
ID=22612529
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US168689A Expired - Lifetime US3186596A (en) | 1962-01-25 | 1962-01-25 | Concrete batch blending control system |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3186596A (en) |
Cited By (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3396870A (en) * | 1967-01-03 | 1968-08-13 | Gen Motors Corp | Mechanical metal pouring control system and components thereof |
| US3609316A (en) * | 1966-05-24 | 1971-09-28 | Pedershaab Maskinfabrik As | Composite mixture batching |
| US3626377A (en) * | 1970-08-11 | 1971-12-07 | Arizona Feeds | Matrix generator for use in solving feed formulation problems |
| US3632018A (en) * | 1968-05-17 | 1972-01-04 | Leeds & Northrup Co | Feed rate control in a cement kiln incorporating dust return |
| US3807807A (en) * | 1971-05-10 | 1974-04-30 | Eastern Cyclone Ind Inc | Feeding device for bulk material to a pneumatic conveying system |
| US3834473A (en) * | 1972-05-25 | 1974-09-10 | Siderurgie Fse Inst Rech | Method to regulate feeding of bulk material |
| US4065030A (en) * | 1975-05-20 | 1977-12-27 | Bison-Werke Bahre & Greten Gmbh & Co. Kg | Apparatus for metering particles containing lignocellulose, such as wood chips or the like, which are to be provided with binders |
| US4180185A (en) * | 1976-12-13 | 1979-12-25 | Hokushin Gohan Kabushiki Kaisha | Weight measuring method of powder in an air flow process and apparatus therefor |
| EP0199884A2 (en) * | 1983-11-07 | 1986-11-05 | Torsten Nikolaus Ljung | Method of producing concrete in a mobile concrete station |
| EP0276882A1 (en) * | 1987-01-20 | 1988-08-03 | Deltracon Deventer B.V. | Method and apparatus for preparing concrete mortar |
| EP0431378A2 (en) * | 1989-12-02 | 1991-06-12 | ELBA-WERK Maschinen-Gesellschaft mbH | Method for measuring moisture content of bulk materials in the batch production of building material compositions |
| US5328787A (en) * | 1993-05-24 | 1994-07-12 | Eastman Kodak Company | Method for assessing and controlling the sensitometric characteristics of photographic products |
| NL9302191A (en) * | 1993-12-15 | 1995-07-03 | Daanen B V Maschf | Method and apparatus for proportioning raw materials to make bricks |
| US5818732A (en) * | 1992-05-08 | 1998-10-06 | Eagle Iron Works | Batch timer initialization for a sand classifying tank |
| US6042258A (en) * | 1996-07-31 | 2000-03-28 | Mbt Holding Ag | Admixture dispensing and concrete mixer monitoring method |
| US6113256A (en) * | 1998-11-09 | 2000-09-05 | General Electric Company | System and method for providing raw mix proportioning control in a cement plant with a fuzzy logic supervisory controller |
| US6120173A (en) * | 1998-11-09 | 2000-09-19 | General Electric Company | System and method for providing raw mix proportioning control in a cement plant with a gradient-based predictive controller |
| US6120172A (en) * | 1998-11-09 | 2000-09-19 | General Electric Company | System and method for providing raw mix proportioning control in a cement plant |
| DE19911060A1 (en) * | 1999-03-12 | 2000-10-19 | Mathis Technik | Process for preparing a mixture of building materials |
| US6211470B1 (en) | 1999-11-22 | 2001-04-03 | Westvaco Corporation | Height measurement apparatus for determining the volume/density of wood chips on a conveyor |
| US6309570B1 (en) * | 1998-01-14 | 2001-10-30 | American Equipment Systems | Vacuum extrusion system for production of cement-based articles |
| US20040128032A1 (en) * | 2000-07-05 | 2004-07-01 | Seiji Nakamura | Controlling ready mixed concrete sludge water |
| US20060287773A1 (en) * | 2005-06-17 | 2006-12-21 | E. Khashoggi Industries, Llc | Methods and systems for redesigning pre-existing concrete mix designs and manufacturing plants and design-optimizing and manufacturing concrete |
| US20120026824A1 (en) * | 2010-07-28 | 2012-02-02 | Gauvin Frederic | Blending scale |
| US20170251847A1 (en) * | 2013-10-11 | 2017-09-07 | Gehl Foods, Llc | Food product dispenser and valve |
| USD839062S1 (en) | 2015-08-28 | 2019-01-29 | Gehl Foods, Llc | Tool |
| US10194763B2 (en) | 2014-08-29 | 2019-02-05 | Gehl Foods, Llc | Food product dispenser and valve |
| USD891188S1 (en) | 2014-08-29 | 2020-07-28 | Gehl Foods, Llc | Food dispenser |
| USD944054S1 (en) | 2014-08-29 | 2022-02-22 | Gehl Foods, Llc | Valve |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2510158A (en) * | 1945-08-18 | 1950-06-06 | Koppers Co Inc | Apparatus for adding liquid to control the bulk density of coking coal |
| US2710715A (en) * | 1950-04-17 | 1955-06-14 | Technicon Chromatography Corp | Automatic fraction collection apparatus |
| US2864537A (en) * | 1956-08-14 | 1958-12-16 | Koppers Co Inc | Bulk density control of coking coal |
| US2880764A (en) * | 1957-05-23 | 1959-04-07 | Technicon Chromatography Corp | Drop volume measuring apparatus |
| US2909303A (en) * | 1957-12-09 | 1959-10-20 | Reserve Mining Co | Ratio control of binder to concentrate |
-
1962
- 1962-01-25 US US168689A patent/US3186596A/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2510158A (en) * | 1945-08-18 | 1950-06-06 | Koppers Co Inc | Apparatus for adding liquid to control the bulk density of coking coal |
| US2710715A (en) * | 1950-04-17 | 1955-06-14 | Technicon Chromatography Corp | Automatic fraction collection apparatus |
| US2864537A (en) * | 1956-08-14 | 1958-12-16 | Koppers Co Inc | Bulk density control of coking coal |
| US2880764A (en) * | 1957-05-23 | 1959-04-07 | Technicon Chromatography Corp | Drop volume measuring apparatus |
| US2909303A (en) * | 1957-12-09 | 1959-10-20 | Reserve Mining Co | Ratio control of binder to concentrate |
Cited By (47)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3609316A (en) * | 1966-05-24 | 1971-09-28 | Pedershaab Maskinfabrik As | Composite mixture batching |
| US3396870A (en) * | 1967-01-03 | 1968-08-13 | Gen Motors Corp | Mechanical metal pouring control system and components thereof |
| US3632018A (en) * | 1968-05-17 | 1972-01-04 | Leeds & Northrup Co | Feed rate control in a cement kiln incorporating dust return |
| US3626377A (en) * | 1970-08-11 | 1971-12-07 | Arizona Feeds | Matrix generator for use in solving feed formulation problems |
| US3807807A (en) * | 1971-05-10 | 1974-04-30 | Eastern Cyclone Ind Inc | Feeding device for bulk material to a pneumatic conveying system |
| US3834473A (en) * | 1972-05-25 | 1974-09-10 | Siderurgie Fse Inst Rech | Method to regulate feeding of bulk material |
| US4065030A (en) * | 1975-05-20 | 1977-12-27 | Bison-Werke Bahre & Greten Gmbh & Co. Kg | Apparatus for metering particles containing lignocellulose, such as wood chips or the like, which are to be provided with binders |
| US4180185A (en) * | 1976-12-13 | 1979-12-25 | Hokushin Gohan Kabushiki Kaisha | Weight measuring method of powder in an air flow process and apparatus therefor |
| EP0199884A2 (en) * | 1983-11-07 | 1986-11-05 | Torsten Nikolaus Ljung | Method of producing concrete in a mobile concrete station |
| EP0199884A3 (en) * | 1983-11-07 | 1987-01-14 | Torsten Nikolaus Ljung | Method of producing concrete in a mobile concrete station |
| EP0276882A1 (en) * | 1987-01-20 | 1988-08-03 | Deltracon Deventer B.V. | Method and apparatus for preparing concrete mortar |
| US4881819A (en) * | 1987-01-20 | 1989-11-21 | Deltracon Deventer B.V. | Method and apparatus for preparing concrete mortar |
| EP0431378A2 (en) * | 1989-12-02 | 1991-06-12 | ELBA-WERK Maschinen-Gesellschaft mbH | Method for measuring moisture content of bulk materials in the batch production of building material compositions |
| EP0431378A3 (en) * | 1989-12-02 | 1991-12-27 | Elba-Werk Maschinen-Gesellschaft Mbh & Co. | Method for measuring moisture content of bulk materials in the batch production of building material compositions |
| US5818732A (en) * | 1992-05-08 | 1998-10-06 | Eagle Iron Works | Batch timer initialization for a sand classifying tank |
| US5328787A (en) * | 1993-05-24 | 1994-07-12 | Eastman Kodak Company | Method for assessing and controlling the sensitometric characteristics of photographic products |
| NL9302191A (en) * | 1993-12-15 | 1995-07-03 | Daanen B V Maschf | Method and apparatus for proportioning raw materials to make bricks |
| US6042258A (en) * | 1996-07-31 | 2000-03-28 | Mbt Holding Ag | Admixture dispensing and concrete mixer monitoring method |
| US6042259A (en) * | 1996-07-31 | 2000-03-28 | Mbt Holding Ag | Admixture dispensing and concrete mixer monitoring system |
| US6309570B1 (en) * | 1998-01-14 | 2001-10-30 | American Equipment Systems | Vacuum extrusion system for production of cement-based articles |
| US6113256A (en) * | 1998-11-09 | 2000-09-05 | General Electric Company | System and method for providing raw mix proportioning control in a cement plant with a fuzzy logic supervisory controller |
| US6120173A (en) * | 1998-11-09 | 2000-09-19 | General Electric Company | System and method for providing raw mix proportioning control in a cement plant with a gradient-based predictive controller |
| US6120172A (en) * | 1998-11-09 | 2000-09-19 | General Electric Company | System and method for providing raw mix proportioning control in a cement plant |
| DE19911060A1 (en) * | 1999-03-12 | 2000-10-19 | Mathis Technik | Process for preparing a mixture of building materials |
| DE19911060C2 (en) * | 1999-03-12 | 2001-04-26 | Mathis Technik | Process for the continuous preparation of a building material mixture |
| US6211470B1 (en) | 1999-11-22 | 2001-04-03 | Westvaco Corporation | Height measurement apparatus for determining the volume/density of wood chips on a conveyor |
| US20040128032A1 (en) * | 2000-07-05 | 2004-07-01 | Seiji Nakamura | Controlling ready mixed concrete sludge water |
| US7114842B2 (en) * | 2000-07-05 | 2006-10-03 | W.R. Grace & Co.-Conn. | Controlling ready mixed concrete sludge water |
| US7386368B2 (en) * | 2005-06-17 | 2008-06-10 | Icrete, Llc | Methods and systems for manufacturing optimized concrete |
| US20080009976A1 (en) * | 2005-06-17 | 2008-01-10 | Icrete, Llc | Methods and systems for manufacturing optimized concrete |
| US20080027583A1 (en) * | 2005-06-17 | 2008-01-31 | Icrete, Llc | Computer-implemented methods for redesigning a pre-existing concrete mix design |
| US20080027685A1 (en) * | 2005-06-17 | 2008-01-31 | Icrete, Llc | Methods for determining whether an existing concrete composition is overdesigned |
| US20080027584A1 (en) * | 2005-06-17 | 2008-01-31 | Icrete, Llc | Computer-implemented methods for re-designing a concrete composition to have adjusted slump |
| US20080066653A1 (en) * | 2005-06-17 | 2008-03-20 | Icrete, Llc | Optimized concrete compositions |
| US20060287773A1 (en) * | 2005-06-17 | 2006-12-21 | E. Khashoggi Industries, Llc | Methods and systems for redesigning pre-existing concrete mix designs and manufacturing plants and design-optimizing and manufacturing concrete |
| US20120026824A1 (en) * | 2010-07-28 | 2012-02-02 | Gauvin Frederic | Blending scale |
| US8974109B2 (en) * | 2010-07-28 | 2015-03-10 | Premier Tech Technologies Ltée | Blending scale |
| US20170251847A1 (en) * | 2013-10-11 | 2017-09-07 | Gehl Foods, Llc | Food product dispenser and valve |
| US10470597B2 (en) * | 2013-10-11 | 2019-11-12 | Gehl Foods, Llc | Food product dispenser and valve |
| US11819147B2 (en) | 2013-10-11 | 2023-11-21 | Gehl Foods, Llc | Food product dispenser and valve |
| US10194763B2 (en) | 2014-08-29 | 2019-02-05 | Gehl Foods, Llc | Food product dispenser and valve |
| USD891188S1 (en) | 2014-08-29 | 2020-07-28 | Gehl Foods, Llc | Food dispenser |
| USD891872S1 (en) | 2014-08-29 | 2020-08-04 | Gehl Foods, Llc | Food dispenser |
| USD944054S1 (en) | 2014-08-29 | 2022-02-22 | Gehl Foods, Llc | Valve |
| USD839062S1 (en) | 2015-08-28 | 2019-01-29 | Gehl Foods, Llc | Tool |
| USD886556S1 (en) | 2015-08-28 | 2020-06-09 | Gehl Foods, Llc | Tool |
| USD887230S1 (en) | 2015-08-28 | 2020-06-16 | Gehl Foods, Llc | Tool |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3186596A (en) | Concrete batch blending control system | |
| JP2602819B2 (en) | Automatic control of flowable material flow by continuous metering device | |
| KR0143227B1 (en) | Device and process for monitoring material flow, and use of the process | |
| US2750144A (en) | Methods and apparatus for controllably dispensing moisture bearing ingredients | |
| KR860001809B1 (en) | Apparatus of checking and controlling humidity for storaging food | |
| US3300193A (en) | Control apparatus for material mixers | |
| JPH0345335B2 (en) | ||
| CN105716987B (en) | A kind of sintering moisture of batch detection and analysis device and its analysis method | |
| US2959932A (en) | Density control apparatus | |
| US3796412A (en) | Apparatus and method for controlling moisture content of granular materials | |
| US3566260A (en) | Method and apparatus for measuring the moisture content of a particulate material including material flow control | |
| US3511412A (en) | Apparatus for discharging particulate material | |
| DE4443053A1 (en) | Method and device for continuous, gravimetric metering and mass flow determination of flowable goods | |
| DE3612282C2 (en) | ||
| SU1291517A1 (en) | Method of automatic measured loading of loose materials to moving railway cars | |
| US3164217A (en) | Weighing device | |
| US3396870A (en) | Mechanical metal pouring control system and components thereof | |
| CN205665131U (en) | Sintering cooperation material moisture detection and analysis device | |
| JPH0890549A (en) | Kneading apparatus of ready-mixed concrete | |
| US3117640A (en) | Apparatus for mixing concrete | |
| GB1265371A (en) | ||
| US1775609A (en) | Apparatus for apportioning the ingredients of mixtures | |
| SU493652A1 (en) | Dispenser control unit | |
| USRE28422E (en) | Moisture measuring and totalizing system | |
| ES385288A1 (en) | Measurement of Rate of Material Flow |