CN102527269A - Continuous production process and equipment for liquid detergent - Google Patents
Continuous production process and equipment for liquid detergent Download PDFInfo
- Publication number
- CN102527269A CN102527269A CN2012100359617A CN201210035961A CN102527269A CN 102527269 A CN102527269 A CN 102527269A CN 2012100359617 A CN2012100359617 A CN 2012100359617A CN 201210035961 A CN201210035961 A CN 201210035961A CN 102527269 A CN102527269 A CN 102527269A
- Authority
- CN
- China
- Prior art keywords
- raw material
- continuous production
- equipment
- liquid detergent
- filling
- 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.)
- Granted
Links
Images
Landscapes
- Accessories For Mixers (AREA)
Abstract
The invention discloses a continuous production process and equipment for liquid detergent, and the process comprise the following steps: continuously and quantificationally adding the raw materials of the liquid detergent into the feeding end of a dynamic mixer at a specific ratio in the formula; finishing corresponding chemical reaction for each raw material component in the dynamic mixer in the process of flowing to an outlet end from an inlet end, and evenly mixing; and then continuously entering filling equipment to generate a liquid detergent finished product. The continuous production equipment disclosed by the invention is combined by equipment and a control system, wherein the equipment is composed of a raw material metering device, conveying equipment, reaction equipment, a detection instrument and an automatic control system. The continuous production equipment has the advantages of simple process, convenience in operation, quickness and flexibility in variety switching and the like; single equipment can produce the liquid detergents of different formulas, product verities can be quickly switched, and the production efficiency and the equipment use ratio are improved.
Description
Technical field
The present invention relates to a kind of commodity production technology and equipment, belong to chemical process and field of mechanical technique, particularly relate to a kind of liquid detergent continuous production processes and equipment.
Background technology
Liquid dishwashing detergent and liquid fabric washing agent have become the standing cleaning supplies in people's life; International and domestic detergent for household use manufacturer mostly has detergent product, and each manufacturer can provide a plurality of detergent product kinds in order to satisfy different consumption demands.But with regard to specific production plant, production equipment is again relatively limited, must on same production equipment, switch the product of producing these One's name is legions, and actual conditions can only be constantly to switch.
As shown in Figure 1; The production technology of liquid detergent all is step at present; In a certain order the raw material in a plurality of raw material storage tanks 1 is added in the agitated reactor 2, and be aided with heating, stirring, homogeneous, cooling and de-foaming process operation in corresponding operation as requested, and then make bulk liquid washing agent semi-finished product; After the quality index detection; Qualified semi-finished product are transported in the temporary cylinder 3 and wait for filling, and are pumped in the filling operation line 5 by filling delivery pump 4, are carried by pipeline 6 at last.The whole production process for preparation is discontinuous, and the output of each agitated reactor is a batch.
Batch production technology also can the implementation part raw material automatic gauge and automatic transport feed intake, some production unit adopts flowmeter metering liquid raw material; The mode that also has production unit to adopt agitated reactor to weigh is metered into the liquid charging stock in the agitated reactor.For solid material and very little in batches liquid charging stock, then need the manually-operated metering to add in the consersion unit with artificial.
Batch production technology also has a distinguishing feature: when each batching finished, batching was produced and has just been stagnated, and needed sampling to carry out quality testing and wait for the quality testing result, and the time of detection also is a part that belongs to the broad sense production time.It is long that the list of batch production technology is criticized the preparation time, and production efficiency and utilization rate of equipment and installations are lower.Batch production technology all will be equipped with the temporary cylinder of semi-finished product feed liquid, and the semi-finished product that are up to the standards need be delivered in the temporary cylinder temporary, wait to be filled.The emptying of agitated reactor this moment prepares to be used for the preparation production of next group product.
Batch production technology is cleared up agitated reactor, temporary cylinder, filling machine and pipeline carrying out stopping to produce batching when kind is switched for a long time.Scale removal process not only can be lost some materials, and the rinse water of labor.
Summary of the invention
In order to overcome the defective that prior art exists; The object of the present invention is to provide a kind of liquid detergent continuous production processes and equipment; Simple, the easy to operate and switching kind fast and flexible of its technology; Can satisfy single equipment and produce the liquid detergent of a plurality of different formulations, the demands of Rapid Realization product variety is enhanced productivity and utilization rate of equipment and installations.
The object of the invention and solve its technical problem and adopt following technical scheme to realize.A kind of liquid detergent continuous production processes according to the present invention proposes may further comprise the steps:
1) detergent raw material that is stored in a plurality of raw material storage tanks adds in the dynamic mixer according to specific ratio through flow measurement device continuously and quantitatively;
2) each raw material components is accomplished corresponding chemical reaction by entrance point and is mixed in port of export process of flowing in dynamic mixer, gets into stowage unit then continuously, output liquid detergent finished product.
In the said step 1), said detergent raw material adding mode is flow morphology; Solid material selects for use solvent to dissolve in advance, and is delivered in the raw material storage tank subsequent use.
Said step 2) in, the raw material after the process dynamic mixer hybrid reaction need be taken into account through online PH and get into the stowage unit conveying again after in-line viscometer measures pH value and viscosity respectively.
Said step 2) in, the product handoff procedure need pick out a certain amount of mixed liquor (mixed liquor that the feed liquid of new preparation produces when the feed liquid of a last kind is released production equipment) from the filling operation line.
In addition, the invention allows for the continuous production equipment of a kind of liquid detergent, it comprises:
Raw material storage tank is used to lay in liquid charging stock;
The raw material metering device; Be connected to the above-mentioned raw materials storage tank; Be used to measure the instant flow of transferring raw material in reactor, the flow of flow signal and default is compared, and then system regulates the rotating speed of corresponding former material conveying pump automatically; The numerical value ratio of the flowmeter behind this raw material conveying capacity of dynamic adjustments and the filling pump, and maintenance and default ratio are consistent;
Reactor is connected to the above-mentioned raw materials metering device, is used for the abundant hybrid reaction of raw material;
Detecting instrument is connected behind the above-mentioned reactor on the pipeline, is used for the pH value and the viscosity of dynamic continuous monitoring filling feed liquid, and viscosity information is presented at field instrument and computer terminal, control room, and system writes down the viscosity data of filling feed liquid continuously and backs up;
Stowage unit and automatic control system are connected behind the above-mentioned detecting instrument on the pipeline; Said control system is according to the viscosity signal, and chain control raw material system medium viscosity is regulated the addition of raw material.
Said raw material metering device comprises first mass flowmenter that is installed on the raw material pipeline, and second mass flowmenter behind the filling pump is installed; Each former material conveying pump basis first quality flowmeter flow quantity thereafter and the ratio variation of second quality flowmeter flow quantity behind the filling pump, corresponding adjustment self rotating speed makes each raw material send into the flow proportional of reactor and the setting value of filling a prescription is consistent.
Said reactor is a dynamic mixer; Said dynamic mixer should have an import and an outlet at least, and said import can connect at least ten raw material storage tank interfaces.
Should not produce pressure in the cavity of said dynamic mixer, comprise that the entrance point and the port of export all do not produce pressure feed liquid; Said dynamic mixer seals fully, does not bring gas in the course of work into, does not make feed liquid produce bubble.
On the pipeline behind the said dynamic mixer bag filter is installed, filter is last endfeed, lower end discharging, three filter bags that evenly distribute in the filter, and filter bag is the inertia material, pore size filter is the 300-500 order.
Said detecting instrument is the on-line continuous detecting instrument, comprises the online pH meter and the in-line viscometer that are connected pipeline after the dynamic mixer, online pH meter and in-line viscometer be connected the sequencing no requirement (NR), exchange the priority position and also can.
By technique scheme, the present invention has following advantage and beneficial effect:
(1) continuous production processes of the present invention is carried out a handover operation needs about 0.5 hour, and general batch production technology needs 4 hours approximately; Continuous production processes can utilize the time of filling field replacement packaging material to accomplish the switching of producing feed proportioning system fully, can extraly not cause damp production.
(2) advantage of continuous production processes is the on-line operation that has realized quality testing, and test items such as pH value and viscosity all detect through the detecting instrument that is installed on the filling pipeline automatically; Contrast batch production technology can be practiced thrift every batch and prepared detection time intermittently; Through measuring and calculating, adopt the factory of batch production technology, need 20 minutes the detection time of every batch of material liquid approximately.
(3) continuous production processes contrast batch production has been saved a feed liquid by the conveying operation of agitated reactor to temporary cylinder, and for about one 10 cubes agitated reactor, this step operation needs 10 minutes at least; Simultaneously, also part has been practiced thrift this step feed liquid and has been carried the material-handling pump of operation use and the power consumption of pipeline.
Description of drawings
Fig. 1 is the flow chart of the batch production technology equipment needed thereby of prior art.
Fig. 2 is the flow chart of the continous way production technology equipment needed thereby of the embodiment of the invention.
Fig. 3 is the flow chart of the continous way production technology equipment needed thereby of another embodiment of the present invention.
1: raw material storage tank 2: agitated reactor 3: temporary cylinder
4: filling delivery pump 5: filling operation line 6: pipeline
10,10 ': raw material storage tank 20,20 ': first mass flowmenter
30,30 ': dynamic mixer 31,31 ': bag filter
40,40 ': online pH meter 50,50 ': in-line viscometer
60,60 ': filling pump 70,70 ': second mass flowmenter
80,80 ': filling operation line 90,90 ': pipeline
The specific embodiment
Below through accompanying drawing and preferred embodiment the present invention is made further detailed presentations, but the present invention is not limited in following embodiment.
See also shown in Figure 2ly, be the structure chart of the continuous production processes equipment needed thereby of liquid detergent of the present invention.It is subsequent use that liquid charging stock directly is delivered to raw material storage tank 10, and it is subsequent use to be delivered to raw material storage tank after solid material need select for use suitable solvent to dissolve in advance.The raw material of liquid detergent measures through first mass flowmenter 20, and adds in the dynamic mixer 30 continuously and quantitatively according to specific ratio.Measure the pH value and the viscosity of material liquids by online pH meter 40 that is connected pipeline after this dynamic mixer 30 and in-line viscometer 50.Be connected to that second mass flowmenter 70 of pipeline is connected to filling operation line 80 after the filling delivery pump 60, carry by the pipelines 90 that are arranged at below the filling operation line 80 at last.According to the scale of raw material in prescription, the parameter of selected proper raw material tank volume, pipe diameter and flowmeter (selecting mass flowmenter for use), the raw material that has reached technological requirement adds precision.
Material rate control principle of the present invention is: system starts according to predefined material rate, and is brought into operation by buffer mode.Automatically in the running; The flow of second mass flowmenter 70 of system after with filling pump 60 serves as to regulate benchmark; Each former material conveying pump basis first mass flowmenter, 20 flows thereafter and the ratio variation of second mass flowmenter, 70 flows behind the filling pump 60; Corresponding adjustment self rotating speed makes each raw material send into the flow proportional of dynamic mixer 30 and the setting value of filling a prescription is consistent, and can satisfy the filling traffic requirement.
The measuring accuracy of above-mentioned mass flowmenter (the present invention does not limit kind, model and the brand of mass flowmenter) is high, and antijamming capability is strong, regulates flexibly, is more suitable for automatic control system.First mass flowmenter 20 on the raw material pipeline is used to measure the instant flow of transferring raw material in dynamic mixer 30; The flow of flow signal and default is compared; And then system regulates the rotating speed of corresponding former material conveying pump automatically; The numerical value ratio of second mass flowmenter 70 behind this raw material conveying capacity of dynamic adjustments and the filling pump 60, and maintenance and default ratio are consistent.The core of source material delivery system is that each raw material additional proportion of control and default ratio are consistent.During the system actual motion, the flow of each raw material is to be associated with the flow of casting resin to calculate.
Above-mentioned dynamic mixer 30 should have an import and an outlet at least, and an import can connect at least ten mother tube interfaces, and the concrete mouthful quantity of taking over is confirmed according to producing the raw material quantity of using.Dynamic mixer 30 can adapt to the lotion that viscosity is arranged, and the lotion range of viscosities is at 100-30000mpa.s (25 ℃).Should not produce pressure in the cavity of dynamic mixer 30, comprise that the entrance point and the port of export all do not produce pressure feed liquid.And dynamic mixer 30 seals fully, does not bring gas in the course of work into, does not make feed liquid produce bubble.
When filling procedure occurs when unusual, the outlet pressure of filling pump 60 will change, and the control system adjusts the rotating speed of filling pump 60 automatically according to the situation of change of filling pump 60 outlet pressures, and then regulates the output flow of filling pump 60.At this moment, second mass flowmenter 70 on the filling pipeline detects changes in flow rate, and the former material conveying pump of associated will be adjusted flow automatically and satisfies the filling demand with it, keeps each raw material and default ratio consistent simultaneously.If filling operation line 80 is shut down, then the filling flow is zero, and system comprises all shutdown simultaneously of source material delivery system and dynamic mixer 30 with autostop.
Continuous production equipment of the present invention comprises: online pH meter 40 is installed on the pipeline behind the dynamic mixer 30; The pH value of online pH meter 40 dynamic continuous detecting filling feed liquids; And the pH value information is presented at field instrument and computer terminal, control room, system writes down the pH Value Data of filling feed liquid continuously and backs up.Automatic control system is according to the pH value signal, and the pH value is regulated the addition of raw material in the chain control raw material system, and the pH value that makes the filling feed liquid is all the time in the pH value scope of product standard regulation.
Continuous production equipment of the present invention comprises: in-line viscometer 50 is installed on the pipeline behind the dynamic mixer; The viscosity of in-line viscometer 50 dynamic continuous detecting filling feed liquids; And viscosity information is presented at field instrument and computer terminal, control room, system writes down the viscosity data of filling feed liquid continuously and backs up.Automatic control system is according to the viscosity signal, and chain control raw material system medium viscosity is regulated the addition of raw material, and the viscosity that makes the filling feed liquid is all the time in the range of viscosities of product standard regulation.
When above-mentioned continuous production processes of the present invention is produced in the switching of reply different formulations product on equipment, has remarkable advantages.At first access next factory formula, and the setting state of should filling a prescription is " using " from system operating computer terminal.The blanking valve open of each raw material storage tank 10 that prescription is corresponding, all the other no material valves then must be closed.Start compounding system, then system begins batching according to the prescription of newly packing into, and the initial flow during start-up system is the 50-60% of metered flow, is one of system's preset parameters.
Through measuring and calculating, continuous production processes of the present invention is carried out a handover operation needs about 0.5 hour, and general batch production technology needs 4 hours approximately.Continuous production processes can utilize the time of filling field replacement packaging material to accomplish the switching of producing feed proportioning system fully, can extraly not cause damp production.
Certainly, need to prove that this handoff procedure also need pick out a certain amount of mixed liquor from filling operation line 80, this part mixed liquor is new preparation, the mixed liquor that when the feed liquid with prescription will go up the feed liquid release production equipment of a kind, will produce.But because continuous production processes does not have feed liquid to keep in cylinder, and process pipe will lack a lot, so the mixed liquor that the contrast batch process produces will lack a lot.
Through measuring and calculating, the each kind of continuous production processes is switched the compound that produces and is about 50 kilograms, and the compound that general batch production technology switching kind once produces is about 200 kilograms.
(dishwashing detergent product continuous production processes and equipment)
Be example with the dishwashing detergent product below, the operating process of using continuous production processes of the present invention is as shown in table 1 below.Comprise normal productive process and the handoff procedure of two products on process units in the table 1.
Two dish washing detergent formula tables of table 1
As shown in Figure 3, be the flowage structure figure of continous way production technology equipment needed thereby of the present invention.The operating process of continuous production processes factory formula one of the present invention can be explained as follows:
Download prescription one by the batching control system operating terminal, and set prescription one for to use state.Open the tremie pipe valve of 1#, 2#, 3#, 4#, 5#, 7#, 8#, 9#, 10#, 12# raw material storage tank 10 ', close 6# and 11# raw material storage tank tremie pipe valve.Bag filter 31 ' is installed on the pipeline behind the dynamic mixer 30 ', and filter is last endfeed, lower end discharging, three filter bags that evenly distribute in the filter, and filter bag is the inertia material, pore size filter is the 300-500 order.
Start feed proportioning system, filling a prescription this moment, relevant feedstock pump, dynamic mixer 30 ', filling delivery pump 60 ', filling machine starts successively in one.System is according to the flow operation 30s of initial setting, and filling this moment pump 60 ' flow is 50% of a metered flow, and system gets into automatic adjustment state then.The initial flow of filling pump 60 ' and filling operation line 80 ' average charging quantity basically identical; The fuselage hopper of filling machine can be brought into play the influence of fluctuations that cushions the filling flow among a small circle; When feed liquid was in above 30% scope of low level in the filling machine hopper, filling pump 60 ' strengthened rotating speed; When feed liquid was in 30% scope below the high position in the filling machine hopper, filling pump 60 ' reduced rotating speed.The filling revolution speed changes the flow that will influence filling pump 60 ' back second mass flowmenter 70 '.The changes in flow rate of second mass flowmenter 70 ' of each former material conveying pump after according to filling pump 60 ', corresponding adjustment self rotating speed, it is consistent to make each raw material send into the flow and the filling flow of dynamic mixer 30 '.Concrete adjustment process is: first mass flowmenter 20 ' behind each former material conveying pump detects material flow; The ratio of system-computed material flow and filling flow; And check mutually with each raw material ratio in prescription, system is the proportional jitter situation in view of the above, regulates the rotating speed of former material conveying pump.
The pH value of online pH meter 40 ' continuous detecting feed liquid, control system are according to the pH value signal, and the pH value is regulated the addition of raw material (acid/alkali) in the chain control raw material system, and the pH value that makes feed liquid is all the time in the pH value scope of product standard regulation.The viscosity of in-line viscometer 50 ' dynamic continuous detecting feed liquid, control system are according to the viscosity signal, and chain control raw material system medium viscosity is regulated the addition of raw material (salt solution etc.), and the viscosity that makes feed liquid is all the time in the range of viscosities of product standard regulation.System gets into even running and automatic adjustment state.
In addition, continuous production processes of the present invention can be explained as follows by the operating process that prescription one switches to prescription two:
When system switches to prescription two products by prescription one product; At first want the executive system shutdown operation; System at first closes each former material conveying pump, dynamic mixer 30 ' and filling delivery pump 60 ', and filling machine moves to shuts down after feed liquid is lower than 10% in the filling machine hopper, and this moment, system stopped fully.The filling workshop begins to carry out filling machine hopper discharge and changes the packaging material operation, carries out each item preparation of filling procedure for next step factory formula two.
Download prescription two by batching automatic control system operating terminal, and set prescription two for to use state.Open the tremie pipe valve of 1#, 2#, 3#, 4#, 6#, 7#, 8#, 9#, 11#, 12# raw material storage tank 10 ', close the tremie pipe valve of 5# and 10# raw material storage tank.
Start feed proportioning system, the operation of this process is identical when filling a prescription a start-up system.But, filling machine need be earlier about 5-10 time filling discharge operation, the mixed liquor in the production equipment is discharged, the quality of two products of avoiding filling a prescription is influenced by prescription residual in the equipment one product.
Discharge operating process and system start the superimposed and counteracting of buffering running, and system gets into normal even running and automatic adjustment state, factory formula two products.
The above; It only is preferred embodiment of the present invention; Be not that the present invention is done any pro forma restriction; Former every technical scheme content of the present invention that do not break away from, all still belongs in the scope of technical scheme of the present invention any simple modification, equivalent variations and modification that above embodiment did according to technical spirit of the present invention.
Claims (10)
1. liquid detergent continuous production processes is characterized in that may further comprise the steps:
1) detergent raw material that is stored in a plurality of raw material storage tanks adds in the dynamic mixer according to specific ratio through flow measurement device continuously and quantitatively;
2) each raw material components is accomplished corresponding chemical reaction by entrance point and is mixed in port of export process of flowing in dynamic mixer, gets into stowage unit then continuously, output liquid detergent finished product.
2. liquid detergent continuous production processes according to claim 1 is characterized in that: in the said step 1), said detergent raw material adding mode is flow morphology; Solid material selects for use solvent to dissolve in advance, and is delivered in the raw material storage tank subsequent use.
3. liquid detergent continuous production processes according to claim 1; It is characterized in that: said step 2), the raw material after the process dynamic mixer hybrid reaction gets into the stowage unit conveying after need measuring pH value and viscosity respectively through online pH meter and in-line viscometer again.
4. liquid detergent continuous production processes according to claim 1 is characterized in that: said step 2), the product handoff procedure need pick out the mixed liquor of a certain amount of new preparation from the filling operation line.
5. continuous production equipment of liquid detergent is characterized in that it comprises:
Raw material storage tank is used to lay in liquid charging stock;
The raw material metering device; Be connected to the above-mentioned raw materials storage tank; Be used to measure the instant flow of transferring raw material in reactor, the flow of flow signal and default is compared, and then system regulates the rotating speed of corresponding former material conveying pump automatically; The numerical value ratio of the flowmeter behind this raw material conveying capacity of dynamic adjustments and the filling pump, and maintenance and default ratio are consistent;
Reactor is connected to the above-mentioned raw materials metering device, is used for the abundant hybrid reaction of raw material;
Detecting instrument is connected behind the above-mentioned reactor on the pipeline, is used for the pH value and the viscosity of dynamic continuous monitoring filling feed liquid, and viscosity information is presented at field instrument and computer terminal, control room, and system writes down the viscosity data of filling feed liquid continuously and backs up;
Stowage unit and automatic control system are connected behind the above-mentioned detecting instrument on the pipeline; Said control system is according to the viscosity signal, and chain control raw material system medium viscosity is regulated the addition of raw material.
6. the continuous production equipment of liquid detergent according to claim 1 is characterized in that: said raw material metering device comprises first mass flowmenter that is installed on the raw material pipeline, and second mass flowmenter behind the filling pump is installed; Each former material conveying pump basis first quality flowmeter flow quantity thereafter and the ratio variation of second quality flowmeter flow quantity behind the filling pump, corresponding adjustment self rotating speed makes each raw material send into the flow proportional of reactor and the setting value of filling a prescription is consistent.
7. the continuous production equipment of liquid detergent according to claim 6 is characterized in that: said reactor is a dynamic mixer; Said dynamic mixer should have an import and an outlet at least, and said import can connect at least ten raw material storage tank interfaces.
8. the continuous production equipment of liquid detergent according to claim 7 is characterized in that: should not produce pressure to feed liquid in the cavity of said dynamic mixer, comprise that the entrance point and the port of export all do not produce pressure; Said dynamic mixer seals fully, does not bring gas in the course of work into, does not make feed liquid produce bubble.
9. the continuous production equipment of liquid detergent according to claim 7; It is characterized in that: on the pipeline behind the said dynamic mixer bag filter is installed; Filter is last endfeed, lower end discharging; Even three filter bags that distribute in the filter, filter bag is the inertia material, pore size filter is the 300-500 order.
10. the continuous production equipment of liquid detergent according to claim 7, it is characterized in that: said detecting instrument is the on-line continuous detecting instrument, comprises being connected the dynamic mixer online pH meter and the in-line viscometer of pipeline afterwards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210035961.7A CN102527269B (en) | 2012-02-16 | 2012-02-16 | Continuous production process and equipment for liquid detergent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210035961.7A CN102527269B (en) | 2012-02-16 | 2012-02-16 | Continuous production process and equipment for liquid detergent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102527269A true CN102527269A (en) | 2012-07-04 |
| CN102527269B CN102527269B (en) | 2014-04-16 |
Family
ID=46336027
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210035961.7A Active CN102527269B (en) | 2012-02-16 | 2012-02-16 | Continuous production process and equipment for liquid detergent |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102527269B (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103908918A (en) * | 2014-04-23 | 2014-07-09 | 四川金堂海纳生物医药技术研究所 | Production process of novel fuel and fabrication method of system device for producing novel fuel |
| CN104338447A (en) * | 2013-08-01 | 2015-02-11 | 上海轻工业研究所有限公司 | On-line solution mixing device and method |
| JP2015081261A (en) * | 2013-10-21 | 2015-04-27 | ライオン株式会社 | Apparatus and method for producing liquid composition |
| CN104826513A (en) * | 2015-05-06 | 2015-08-12 | 中国中轻国际工程有限公司 | Liquid detergent continuous batching apparatus |
| CN104959069A (en) * | 2015-06-19 | 2015-10-07 | 合肥迈拓新材料技术有限公司 | Multi-liquid and multi-channel mixing device |
| CN106244360A (en) * | 2016-09-18 | 2016-12-21 | 广州立白企业集团有限公司 | A kind of liquid detergent serialization process of flexible production and equipment |
| CN107537337A (en) * | 2017-09-20 | 2018-01-05 | 广东丽臣奥威实业有限公司 | A kind of surfactant dilution process |
| CN109513416A (en) * | 2018-12-28 | 2019-03-26 | 广州立白企业集团有限公司 | A kind of liquid detergent pipeline hybrid system |
| CN113960267A (en) * | 2021-12-20 | 2022-01-21 | 东营科宏化工有限公司 | Quality analysis device for o-tert-butylcyclohexyl acetate synthetic perfume |
| US11925912B2 (en) | 2016-03-11 | 2024-03-12 | Fujifilm Electronic Materials U.S.A., Inc. | Fluid processing systems including a plurality of material tanks, at least one mixing tank, at least one holding tank, and recirculation loops |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005307069A (en) * | 2004-04-23 | 2005-11-04 | Lion Corp | Method for producing liquid composition and method for filling the same |
| CN101869812A (en) * | 2009-04-23 | 2010-10-27 | 株式会社东进世美肯 | Chemical composition preparation device using continuous mixing device |
| CN202478933U (en) * | 2012-02-16 | 2012-10-10 | 广州立白企业集团有限公司 | Continuous production equipment for liquid detergent |
-
2012
- 2012-02-16 CN CN201210035961.7A patent/CN102527269B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005307069A (en) * | 2004-04-23 | 2005-11-04 | Lion Corp | Method for producing liquid composition and method for filling the same |
| CN101869812A (en) * | 2009-04-23 | 2010-10-27 | 株式会社东进世美肯 | Chemical composition preparation device using continuous mixing device |
| CN202478933U (en) * | 2012-02-16 | 2012-10-10 | 广州立白企业集团有限公司 | Continuous production equipment for liquid detergent |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104338447A (en) * | 2013-08-01 | 2015-02-11 | 上海轻工业研究所有限公司 | On-line solution mixing device and method |
| JP2015081261A (en) * | 2013-10-21 | 2015-04-27 | ライオン株式会社 | Apparatus and method for producing liquid composition |
| CN103908918A (en) * | 2014-04-23 | 2014-07-09 | 四川金堂海纳生物医药技术研究所 | Production process of novel fuel and fabrication method of system device for producing novel fuel |
| CN104826513A (en) * | 2015-05-06 | 2015-08-12 | 中国中轻国际工程有限公司 | Liquid detergent continuous batching apparatus |
| CN104959069B (en) * | 2015-06-19 | 2017-06-23 | 合肥迈拓新材料技术有限公司 | Many liquid multichannel mixing arrangements |
| CN104959069A (en) * | 2015-06-19 | 2015-10-07 | 合肥迈拓新材料技术有限公司 | Multi-liquid and multi-channel mixing device |
| US11925912B2 (en) | 2016-03-11 | 2024-03-12 | Fujifilm Electronic Materials U.S.A., Inc. | Fluid processing systems including a plurality of material tanks, at least one mixing tank, at least one holding tank, and recirculation loops |
| CN106244360A (en) * | 2016-09-18 | 2016-12-21 | 广州立白企业集团有限公司 | A kind of liquid detergent serialization process of flexible production and equipment |
| CN106244360B (en) * | 2016-09-18 | 2019-06-04 | 广州立白企业集团有限公司 | A kind of liquid detergent serialization process of flexible production and equipment |
| CN107537337A (en) * | 2017-09-20 | 2018-01-05 | 广东丽臣奥威实业有限公司 | A kind of surfactant dilution process |
| CN109513416A (en) * | 2018-12-28 | 2019-03-26 | 广州立白企业集团有限公司 | A kind of liquid detergent pipeline hybrid system |
| CN113960267A (en) * | 2021-12-20 | 2022-01-21 | 东营科宏化工有限公司 | Quality analysis device for o-tert-butylcyclohexyl acetate synthetic perfume |
| CN113960267B (en) * | 2021-12-20 | 2022-03-18 | 东营科宏化工有限公司 | Quality analysis device for o-tert-butylcyclohexyl acetate synthetic perfume |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102527269B (en) | 2014-04-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102527269B (en) | Continuous production process and equipment for liquid detergent | |
| JP7429699B2 (en) | Calibration method for liquid flow meters | |
| CN202478933U (en) | Continuous production equipment for liquid detergent | |
| CN214915624U (en) | Automatic change batching slurrying device | |
| CN102806027B (en) | Multichannel mixing system and liquid on-line hybrid system | |
| CN103273582B (en) | The static mixing system of a kind of High Precision Automatic weight-loss type and method for mixing thereof | |
| CN205905249U (en) | Hybrid system is carried to multicomponent raw materials | |
| CN209508114U (en) | A kind of chloroethylene polymerization initiator addition system | |
| CN106244360B (en) | A kind of liquid detergent serialization process of flexible production and equipment | |
| CN207268843U (en) | A kind of band measures continuous loading and unloading system | |
| CN107029622A (en) | Urethane raw high-precision measuring mixing equipment | |
| CN204107351U (en) | Automatic blending is high stirs cold mixing system | |
| CN202087289U (en) | Multi-path liquid mixing system and liquid on-line mixing system | |
| CN109144001A (en) | A kind of waterglass automated production monitoring system | |
| CN201926491U (en) | Weight loss type powder and liquid continuous weighing platform scale device | |
| CN207287340U (en) | A kind of feeding system for further improving chemical industry slurry consecutive production charge ratio precision | |
| CN106426615B (en) | The online mixing equipment of polyethers continous way | |
| CN206810192U (en) | Urethane raw high-precision measuring mixing equipment | |
| CN206625025U (en) | One kind washing bleaching machine auto feed feed supplementing device | |
| CN201986661U (en) | Automatic liquid preparing adding device in feed mill | |
| CN211051415U (en) | Intelligent additive masterbatch batching system | |
| CN204522939U (en) | A kind of concrete additive processing unit (plant) | |
| CN201833478U (en) | Adding device for liquid admixture | |
| TWI396952B (en) | Automatic production system for continuous measurement of output and production and the method thereof | |
| CN211159588U (en) | Efficient and intelligent additive compounding device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |