CN102531327A - Automatic compound conditioning device and conditioning method for sludge dewatering - Google Patents
Automatic compound conditioning device and conditioning method for sludge dewatering Download PDFInfo
- Publication number
- CN102531327A CN102531327A CN2011104559355A CN201110455935A CN102531327A CN 102531327 A CN102531327 A CN 102531327A CN 2011104559355 A CN2011104559355 A CN 2011104559355A CN 201110455935 A CN201110455935 A CN 201110455935A CN 102531327 A CN102531327 A CN 102531327A
- Authority
- CN
- China
- Prior art keywords
- amendment
- conditioning
- liquid
- jar
- mud
- 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
- Treatment Of Sludge (AREA)
Abstract
The invention relates to the technical field of a sludge dewatering device, and discloses an automatic compound conditioning device and a conditioning method for sludge dewatering. The device comprises a conditioning tank, a plurality of liquid conditioner feeding systems, a plurality of solid conditioner feeding systems, a control system and a stirring system, wherein the conditioning tank can contain sludge which needs to be conditioned; the control system can respectively and correspondingly control the liquid conditioner feeding systems and the solid conditioner feeding systems to complexly feed liquid conditioner and solid conditioner to the conditioning tank; and the stirring system stirs sludge in the conditioning tank and respectively stirs the liquid conditioner in the liquid conditioner feeding systems. In the whole sludge conditioning process, the control system comprehensively controls the liquid conditioner feeding system completely according to the setting of a preset program, and various different liquid conditioners and solid liquid conditioners can be complexly fed simultaneously or in sequence according to the practical requirement. The automatic compound conditioning device has the advantages of high automation degree and high working efficiency and is convenient to operate, and high cost can be lowered.
Description
Technical field
The present invention relates to the technical field of sludge dehydration device, relate in particular to automatic compound conditioning system of sludge dewatering and Opsonizing method thereof.
Background technology
Quickening of urbanization process causes the sharp increase of sludge quantity, and mud granule is tiny, and wetting ability is extremely strong, water ratio is up to 95%~99%, therefore, handle mud, just must dewater to mud earlier.Moisture in the mud generally is divided into four kinds of existence forms: interstitial water 70%, capillary water 20%, planar water and mud granule internal water 10%, general mechanical dehydration are difficult to the internal water of the capillary water in the mud, planar water and mud granule is removed.
At present, before carrying out sludge dewatering, must carry out physics, chemical conditioning to mud earlier,, be convenient to subsequent disposal to improve the dewatering of mud.In the conventional art, adopt single polymeric flocculant that mud is nursed one's health, the moisture content of the cake after the conditioning has brought difficulty for follow-up disposal such as mud sanitary landfill, burning up to about 80%.
The Sludge Chemical Conditioning agent is according to the difference of their mechanism of action; Generally comprise following type: one, polymeric flocculant, SEPIGEL 305 (PAM) is the most commonly used, and its mechanism of action is the effect through adsorption bridging; The mud small-particle is connected into macrobead, improve the settling property of mud; Two, inorganic salt high-valence cationic coagulating agent, the high-valence cationic that this coagulating agent hydrolysis forms plays the effect of surperficial water layer (electrostatic double layer) thickness of direct compression mud granule with the negative charge on the mud granule attracts each other and electrically neutralization; Three, coagulant aids, itself does not generally play coagulation, and the pH value that is to regulate mud is supplied with mud with the holey skeleton, improves the mud granule structure, destroys mud colloidal stability, improves the coagulation effect of coagulating agent, strengthens flco intensity; Four, tensio-active agent; Its solublization and dissemination have changed the size and the hydrophilic and hydrophobic of mud flco; Make the part combination water change into free water, the association of its hydrophobic structure destroys the colloidal open structure of mud flco, makes the Sludge Surface hydrophobization; Capillary combination water and surface adsorption water all are able to remove, thereby improve dewatering performance of sludge; Five, oxygenant through the effect of oxygenant and mud flco, destroys the hydrophilic-structure of extracellular polymeric (EPS) in the mud, makes the part combination water change into free water, thereby improves the dewatering of mud.
In actually operating; Use single Sludge Chemical Conditioning agent often to be difficult to reach the purpose of deeply dehydrating sludge; In order further to reduce the water ratio of the mud after the processed, generally adopt compound amendment or with the composite use of amendment, to improve the dewatering of mud.And in compound conditioning system, operating parameterss such as the dosage of each amendment, order of adding, churning time, stirring velocity and reaction times are vital to the final effect of conditioning.Compound conditioning technology to comprise extracellular polymeric in the mud (EPS) dissolving step is an example; Potential of hydrogen must accurately be controlled on the time at stirring reaction; If it is too fast that the alkali solid powder adds; Sludge system will carry out the transition to alkalescence from acidity in advance, and the extracellular polymeric dissolving is not thorough, and the improvement degree of dewatering performance of sludge is not ideal enough; If it is slow that the alkali solid powder added, or mix inhomogeneous, the extracellular polymeric dissolved simultaneously, mikrobe is dissolved the mutual down dispersion of effect in acid, the mud flco is tiny, settling property is poor, is unfavorable for moisture removal.
In the prior art, in the sludge dewatering conditioning device, the amendment that is used for sludge dewatering still needs the manual operation dosing, can't realize robotization control, its inefficiency, and the wasting manpower and material resources, cost is high, its holistic management and inconvenient operation.
Summary of the invention
The object of the present invention is to provide the automatic compound conditioning system of sludge dewatering, be intended to solve that sludge dewatering conditioning device of the prior art can't operate automatically that amendment, level of automation are low, inefficiency, cost is high and unhandy problem.
The present invention realizes like this; The automatic compound conditioning system of sludge dewatering, comprise the mud that is used for holding the needs conditioning conditioning jar, several liquid amendment medicine systems, several solid-state amendment medicine systems, can the corresponding respectively said liquid amendment medicine system of control and said solid-state amendment medicine system drive the stirring system that the mud to said conditioning jar stirs and respectively the liquid amendment in said several liquid amendment medicine systems stirred to the system of said conditioning jar liquid amendment of compound filling and solid-state amendment and by said system.
Further, comprise also and can detect and control the measuring element that said system starts that said measuring element is located at said conditioning jar to a said conditioning jar interior mud liquid level.
Further; Said conditioning jar be provided with can supply mud get in the said conditioning jar advance the mud pipe and can supply to nurse one's health after mud discharge a said conditioning jar outer sludge out pipe; Saidly advance the mud pipe coupling dredge pump that advances by said system control operation is arranged; Its pipeline is provided with and can closes or open the said Mud-intake valve door that advances the mud pipe by the control of said system; Said sludge out pipe is connected with the shell pump by said system control operation, and its pipeline is provided with the mud extraction valve that can be closed or opened said sludge out pipe by said system control.
Further; But each said liquid amendment medicine system comprises and is used to hold the liquid amendment jar of liquid amendment, is communicated with said conditioning jar and said liquid amendment jar and feed flow attitude amendment respectively and gets into and advance the agent pipe in the said conditioning jar; And be communicated with said liquid amendment jar and can supply outside liquid amendment to get into and add the agent pipe in the said liquid amendment jar, the said pipeline that advances the agent pipe be provided with can by the agent-entering pump of said system control operation and can by said system control close or open said advance the agent pipe advance the agent valve.
Further, each said solid-state amendment medicine system comprises the feeder that is communicated with said conditioning jar and is used to hold solid-state amendment, is communicated with said feeder and is used for the hopper of the solid-state amendment of filling in the said feeder and can be driven solid-state amendment filling to the said conditioning jar first interior power spare in the said feeder by said system.
Further, said stirring system comprises and places in the said conditioning jar and can driven first mixing component that the mud in the said conditioning jar is stirred and placed in the said liquid amendment jar and can drive second mixing component that the liquid amendment in the said liquid amendment jar is stirred by said system by said system.
Further; Said system comprises the upper computer of the pre-set programs that can deposit external setting-up in and by the lower computer of said PC control, said lower computer is electrically connected at liquid amendment medicine system, solid-state amendment medicine system and stirring system respectively.
Further, any one or a few of the SEPIGEL 305 that said liquid amendment is the solution form or sulfuric acid or ferric sulfate, said solid-state amendment are any one or a few of flyash or terra alba or cement of powder fine aggregate form.
The present invention also provides the Opsonizing method of the automatic compound conditioning system of sludge dewatering, and is specific as follows:
The pre-set programs of external setting-up is deposited to system;
Annotate respectively in several liquid amendment medicine systems and several solid-state amendment medicine systems respectively liquid amendment and solid-state amendment;
Toward the conditioning jar mud that interior filling must be nursed one's health;
Said system starts stirring system to being opposite to said conditioning jar interior mud respectively and placing the liquid amendment in said several liquid amendment medicine systems to stir;
Said system is controlled said several liquid amendment medicine systems and said several solid-state amendment medicine systems liquid amendment of compound filling and solid-state amendment in the said conditioning jar respectively;
Said system starts said stirring system the mud of annotate liquid amendment and solid-state amendment is stirred;
The mud that stirs is discharged outside the said conditioning jar.
Further; Respectively in the said conditioning jar in the process of liquid amendment of compound filling and solid-state amendment, said system is controlled said several liquid amendment medicine systems and said several solid-state amendment medicine systems the annotate filling rate and the filling order of liquid amendment and solid-state amendment respectively in said several liquid amendment medicine systems and said several solid-state amendment medicine systems.
Further, after outside the said conditioning jar of the mud discharge that stirs, the automatic compound conditioning system of said sludge dewatering brings into operation again automatically.
Further, said stirring system is 100r/min~400r/min to the stirring velocity scope that the mud of the amendment of not annotating stirs, and the time range that the mud of filling amendment is stirred is 10min~60min.
Further, to be opposite to the stirring velocity scope of the liquid amendment in said several liquid amendment medicine systems be 50r/min~500r/min to said stirring system.
Compared with prior art, operator can weave preset program in advance according to the processing needs to mud; And pre-set programs deposited to system, and liquid amendment of filling and solid-state amendment in several liquid amendment chemicals dosing plants and several solid-state amendment chemicals dosing plants respectively, and the mud that needs carry out processed is filled in the conditioning jar; Under the control of system, stirring system can carry out stir process to mud and liquid amendment, and according to pre-set programs; Liquid amendment and solid-state amendment are filled in the mud, and stirring system stirs the mud of annotated liquid amendment and solid-state amendment once more, and is last; Mud after the conditioning is discharged outside the conditioning jar, to carry out next step dehydration operation, in this whole process; System is controlled according to the setting of pre-set programs fully comprehensively, realizes operating automatically the filling of liquid amendment and solid-state amendment, its level of automation height and high efficiency; The height that can reduce cost is operated also very convenient.
Description of drawings
The work simplified schematic diagram of the automatic compound conditioning system of sludge dewatering that Fig. 1 provides for the embodiment of the invention;
Embodiment
In order to make the object of the invention, technical scheme and advantage clearer,, the present invention is further elaborated below in conjunction with accompanying drawing and embodiment.Should be appreciated that specific embodiment described herein only in order to explanation the present invention, and be not used in qualification the present invention.
The invention provides the automatic compound conditioning system of sludge dewatering, comprise the mud that is used for holding the needs conditioning conditioning jar, several liquid amendment medicine systems, several solid-state amendment medicine systems, can the corresponding respectively said liquid amendment medicine system of control and said solid-state amendment medicine system drive the stirring system that the mud to said conditioning jar stirs and respectively the liquid amendment in said several liquid amendment medicine systems stirred to the system of said conditioning jar liquid amendment of compound filling and solid-state amendment and by said system.
The automatic compound conditioning device of sludge dewatering of the present invention can be realized robotization control, and its level of automation is high, and high efficiency does not need operator's participation in the operating process, and cost is low, and easy to operate.
Below in conjunction with concrete accompanying drawing detailed description is carried out in realization of the present invention.
As shown in Figure 1, be a preferred embodiment provided by the invention.
The automatic compound conditioning system 1 of sludge dewatering in the present embodiment; Dosage, order of adding, churning time, stirring velocity and the reaction times that can be used for polytype amendment are controlled automatically; Make that the amendment of number of different types is compound to the mud effect; Reaching preferable sludge conditioning effect, and for mud to carry out next step dehydration ready.
Automatic compound conditioning system 1 comprises system 10, be used for conditioning jar 13, several liquid amendment medicine systems 12, several solid-state amendment medicine system 11 and stirring systems of the mud that device need nurse one's health, and system 10 is as the Master Control Center of whole automatic compound conditioning system 1, and it is according to the predefined program of operator; Operation to whole automatic compound conditioning system 1 is controlled; Conditioning jar 13 is used for the mud that device need be nursed one's health, and the mud that need get into should be nursed one's health after the jar 13, under the processing of polytype amendment; Nurse one's health; After conditioning finishes, from conditioning jar 13, discharge again, so that follow-up further deep dehydration; New mud continues to get in the conditioning jar 13, the conditioning of a beginning new round; Several liquid amendment medicine systems 12 are used for to the conditioning jar liquid amendment of 13 addings, certainly, in the whole process that adds liquid amendment, 10 controls of the complete controlled system of its operation behavior; Several solid-state amendment medicine systems 11 are used for to the conditioning jar solid-state amendment of 13 addings, certainly, in the whole process that adds solid-state amendment, 10 controls of the complete controlled system of its operation behavior; Stirring system is under the control of system 10; Be responsible for the mud of nursing one's health in the jar 13 is stirred, make the amendment that adds in the conditioning jar 13 to nurse one's health, simultaneously mud; Also the liquid amendment in the liquid towards amendment medicine system 12 stirs, and guarantees that also liquid amendment is even.In addition; System 10 can be distinguished the liquid amendment medicine system 12 of corresponding control and solid-state amendment medicine system 11 to conditioning jar a liquid amendment of 13 compound filling and solid-state amendments; Here " compound filling " refers to: by the control of system 10, several liquid amendment medicine systems 12 can while or the random order corresponding liquid amendment of filling and solid-state amendment in conditioning jar 13 with several solid-state amendment medicine systems 11.
Be provided with cavity volume 132 in the conditioning jar 13 in above-mentioned; This cavity volume 132 is used for the mud that device need be nursed one's health, and certainly, what the upper end of this conditioning jars 13 was provided with communicating vessels inner volume 132 advances mud pipe 136 and sludge out pipe 133; The mud that outside need is nursed one's health can pass through this and advance mud pipe 136 and enter into the cavity volume 132 in the conditioning jars 13; After the mud in the cavity volume 132 is through conditioning, then can flow to the outside, so that follow-up further deep dehydration via sludge out pipe 133.
Certainly, above-mentioned liquid amendment medicine system 12 and solid-state amendment medicine system 11 also are communicated with the cavity volume 132 of conditioning jar 13 inside respectively, thereby under the control of system 10, can nurse one's health in the jar 13 in the past and add liquid amendment and solid-state amendment.
In the present embodiment; For the ease of controlling in 10 pairs of mud entering of system conditioning jar 13; Advance mud pipe 136 and be provided with into dredge pump 137; And its pipeline is provided with can close or open the into Mud-intake valve door 138 of mud pipe 136, and this advances dredge pump 137 and is electrically connected at respectively on the system 10 with Mud-intake valve door 138, and is started or closed by system 10 controls.
Certainly; For the ease of controlling through the discharge of the mud after the conditioning in 10 pairs of conditioning jars 13 of system; Sludge out pipe 133 is provided with shell pump 134; And its pipeline is provided with the mud extraction valve 135 that can close or open sludge out pipe 133, and this shell pump 134 is electrically connected at respectively on the system 10 with mud extraction valve 135, and is started or closed by system 10 controls.
Liquid amendment medicine system 12 in above-mentioned comprises the liquid amendment jar 121 that is used for the liquid amendment of device, be communicated with this liquid state amendment jar 121 and be communicated with simultaneously conditioning jars 13 advance agent pipe 122 and be communicated with this liquid state amendment jar 121 and be used in the liquid amendment jar 121 liquid amendments of filling add agent pipe 125.Get in the conditioning jar 13 via advancing agent pipe 122 for the ease of the liquid amendment in the liquid amendment jar 121; This end that advances agent pipe 122 is arranged on the lower end of liquid amendment jar 121; The other end is arranged on the upper end of conditioning jar 13; Equally, for the ease of in liquid amendment jar 121, pouring into amendment, add the upper end that agent pipe 125 is arranged on liquid amendment jar 121 in above-mentioned.
Certainly; In order to make the liquid state in the liquid amendment jar 121 nurse one's health toward the control of nursing one's health the controlled system 10 of the liquid amendment of filling in the jar 13; In advancing agent pipe 122, be provided with agent-entering pump 123, and its pipeline is provided with into agent valve 124, this agent-entering pump 123 can be taken out the liquid amendment in the liquid amendment jar 121 in the conditioning pipe; Advance agent valve 124 and can close or open into agent pipe 122; Thereby make liquid amendment be filled in the conditioning jars 13 or stop liquid amendment to be filled in the conditioning jars 13, this agent-entering pump 123 with advance agent valve 124 and all be electrically connected on the system 10, control by this system 10.
Solid-state amendment medicine system 11 in above-mentioned comprises and is communicated with the inner and device of conditioning jars 13 feeder 111 of solid-state amendment is arranged, can make the solid-state amendment in the feeder 111 to be filled into the first power spare 113 in the conditioning jars 13 and is arranged on the feeder 111 and the hopper 112 of the solid-state amendments of can annotating in the feeder 111; The first power spare 113 in above-mentioned is electrically connected in the system 10; By system 10 control operations; Thereby the solid-state amendment filling in the realization system 10 control feeders 111 is in conditioning jar 13; After the solid-state amendment in the feeder 111 uses; The operator can directly add solid-state amendment in hopper 112, make solid-state amendment be filled in the feeder 111.
In the present embodiment, stirring system comprises and is arranged in the conditioning jars 13 first mixing component that can be stirred the mud in the conditioning jars 13 by system 10 controls and is arranged on liquid amendment jar 121 and can drives second mixing component that the liquid amendment that is placed in the liquid amendment jar 121 is stirred by system 10.
Particularly; First mixing component comprises and can and be arranged in the conditioning jars 13 and can drive first agitating member that stirs by the second power spare 143 by the second power spare 143 of system 10 control operation; Like this; After system 10 was sent the stirring signal, 143 of the second power spares can drive first agitating member and stir being placed on conditioning jar 13 interior mud.
Certainly; First agitating member in above-mentioned comprises first agitator arm 142 that is rotated by 143 drivings of the second power spare and first agitating vane 141 that is arranged on first agitator arm, 142 1 ends, is realized conditioning jar 13 interior mud are stirred by this first agitating vane 141.
Particularly; Second mixing component comprises and can and be arranged in the liquid amendment jar 121 and can drive second agitating member that stirs by the 3rd power spare 146 by the 3rd power spare 146 of system 10 control operation; Like this; After system 10 was sent the stirring signal, 146 of the 3rd power spares can drive second agitating member liquid amendments that are placed in the liquid amendment jar 121 are stirred.
Certainly; Second agitating member in above-mentioned comprises second agitator arm 145 that is rotated by 146 drivings of the 3rd power spare and second agitating vane 144 that is arranged on second agitator arm, 145 1 ends, realizes that by this second agitating vane 144 the liquid amendments in liquid towards amendment jars 121 stir.
Certainly; Owing in the lower computer 102 PLC is arranged; In order to realize the control of this PLC liquid towards amendment medicine system 12 and solid-state amendment medicine system 11; This system 10 also comprises rly. 104, and lower computer 102 is electrically connected at respectively on liquid amendment medicine system 12 and the solid-state amendment medicine system 11 through rly. 104, promptly through rly. 104 respectively to advancing the control of agent valve 124, Mud-intake valve door 138 and mud extraction valve 135.
In the present embodiment, the first power spare 113, the second power spare 143 and the 3rd power spare 146 in above-mentioned are motor, certainly, also can be other various forms of power spares.
Certainly, in the process that mud is nursed one's health, need use multiple amendment, so, include two liquid amendment medicine systems 12 and two solid-state amendment medicine systems 11 in the automatic compound conditioning system 1 in above-mentioned.
In the present embodiment; Automatic compound conditioning system 1 also comprises the measuring element 15 that can detect mud liquid level in the conditioning jar 13, and this measuring element 15 is arranged on the conditioning jar 13, and is communicated with the cavity volume 132 in the conditioning jar 13; Like this; Be convenient to it liquid level that is placed on the mud in the conditioning jar 13 is detected, this measuring element 15 electrically connects system 10, by the liquid level situation of its mud in system 10 is transmitted conditioning jar 13.
Certainly; In order to realize whole robotizations; This measuring element 15 can also be controlled the startup of system 10; When the liquid level of the mud in jar 13 is being nursed one's health in filling reached and presets liquid level, this measuring element 15 can send signal to system 10 simultaneously, made this system 10 start and carried out the sequence of operations of conditioning operation to nursing one's health jar 13 interior mud.
In the present embodiment, liquid amendment can be any one or a few of solution such as SEPIGEL 305 (PAM), sulfuric acid, ferric sulfate, as required, can also be other multiple liquid solution.
Solid-state amendment can be any one or a few of the flyash of powder fine aggregate form, terra alba, cement dust etc., as required, can also be other multiple solid bodies.
The present invention also provides the Opsonizing method of the automatic compound conditioning system 1 of sludge dewatering, and is specific as follows:
Operator are the preset program of input in system 10 as required, and this program can be controlled total system, and promptly liquid towards amendment medicine system 12, solid-state amendment medicine system 11 and stirring system are controlled;
Respectively in several liquid amendment medicine systems 12 and several solid-state amendment medicine systems 11 corresponding filling by required liquid amendment and the solid-state amendment of pre-set programs;
Toward nursing one's health the mud that filling need be nursed one's health in the jar 13;
Start stirring system, respectively the mud of conditioning jar 13 and the mud in the liquid amendment medicine system 12 are carried out stir process;
According to the setting of pre-set programs, respectively toward nursing one's health liquid amendment of compound filling and solid-state amendment in the jar 13;
Start stirring system, the mud of annotated liquid amendment and solid-state amendment is stirred, carry out stirring operation according to the churning time of pre-set programs;
After the mud of liquid amendment and solid-state amendment of having annotated in above-mentioned stirs and to finish, it is discharged conditioning jars 13, the automatic compound conditioning system 1 of sludge dewatering gets into the operation of next round again.
In above-mentioned; Both can be simultaneously annotate respectively in several liquid amendment medicine systems 12 and several solid-state amendment medicine systems 11 required liquid amendment and solid-state amendment; Also can successively annotate, certainly, also can separate a time period according to the program needs.
Same reason can also can successively be annotated simultaneously respectively toward nursing one's health liquid amendment of filling and solid-state amendment in the jar 13, perhaps separates a time period, and specifically filling situation is looked practical situation and decided.
In the above-mentioned whole process that mud is nursed one's health, out of service when system 10, then this automatic compound conditioning system 1 is accomplished after the circulation, can not get into next circulation automatically again, necessary manual activation; Certainly, when system 10 does not stop, this automatic compound conditioning system 1 constantly cyclical operation goes down.
In the present embodiment; In liquid amendment medicine system 12 and solid-state amendment medicine system 11 are annotated the process of liquid amendment and solid-state amendment respectively in the conditioning jars 13; System 10 can be controlled the filling rate and the filling order of liquid amendment medicine system 12 and solid-state amendment medicine system 11 liquid amendments of filling and solid-state amendment respectively; The churning time of 10 pairs of stirring systems of system and the control of speed can be looked material different and difference, and is unfixing; In like manner, the control of liquid towards amendment medicine system 12 and solid-state amendment medicine system 11 for example adds dose, administration timing of drug or the like, can be according to different amendments and difference, and fixing.
In the present embodiment, the stirring velocity scope that stirring system stirs the mud of the amendment of not annotating is for being generally 100r/min~400r/min, and the time range that the mud of filling amendment is stirred is 10min~60min; The stirring velocity scope that this stirring system is opposite to the liquid amendment in the liquid amendment medicine system 12 is 50r/min~500r/min.Certainly, other multiple parameter of being controlled by system 10 can also be arranged, the difference of the concrete amendment that visual reality is set and difference.
Below the composite conditioner formed with terra alba and SEPIGEL 305 (PAM) be example, the Opsonizing method of the automatic compound conditioning system 1 of sludge dewatering is described.
Deposit the pre-set programs that presets in the upper computer 101 in system 10, it can control the delivery rate of feeder 111 and the stirring velocity of stirring system etc.;
Through adding agent pipe 125 good certain density SEPIGEL 305 (PAM) solution of filling configured in advance in the liquid amendment jar 121, through hopper 112 terra alba of in feeder 111, annotating;
Open Mud-intake valve door 138 and advance dredge pump 137, make extraneous mud can enter into conditioning jars 13, after advancing mud and finishing, start first mixing component, this first mixing component stirs the mud in the conditioning jars 13, and its stirring velocity is 300r/min;
The liquid amendment that starts in the second mixing component liquid towards amendment jar 121 carries out stir process, and its stirring velocity is 150r/min, and churning time is set to 25min;
Start and advance agent valve 124 and agent-entering pump 123, make that the liquid amendment in the liquid amendment jar 121 is filled in the conditioning jar 13;
Start the first power spare 113, make that the solid-state amendment in the feeder 111 is filled in the conditioning jar 13, the velocity of rotation of setting the first power spare 113 is 15r/min, and be 33s working time;
First mixing component of startup stirring system stirs the mud of annotated SEPIGEL 305 (PAM) and terra alba, and the setting churning time is 45min, thereby, mud is nursed one's health;
After sludge conditioning finishes, will discharge from sludge out pipe 133 roads on the conditioning jar 13 through the mud of conditioning, so that follow-up further deep dehydration.
Below the composite conditioner formed with sulfuric acid, ferric sulfate, flyash and concrete grey be example, the Opsonizing method of the automatic compound conditioning system 1 of sludge dewatering is described.
Deposit the pre-set programs that presets in the upper computer 101 in system 10, it can control the delivery rate of feeder 111 and the stirring velocity of stirring system etc.;
Through adding agent pipe 125 good certain density sulphuric acid soln and ferrum sulfuricum oxydatum solutum of filling configured in advance in the liquid amendment jar 121, through hopper 112 in feeder 111, annotate flyash and cement dust;
Open Mud-intake valve door 138 and advance dredge pump 137, make extraneous mud can enter into conditioning jars 13, after advancing mud and finishing, start first mixing component, this first mixing component stirs the mud in the conditioning jars 13, and the setting stirring velocity is 200r/min;
The liquid amendment that starts in the second mixing component liquid towards amendment jar 121 carries out stir process, and the setting stirring velocity is 120r/min;
Start and advance agent valve 124 and agent-entering pump 123, make that the liquid amendment in the liquid amendment jar 121 is filled in the conditioning jar 13;
Start the first power spare 113, make that the solid-state amendment in the feeder 111 is filled in the conditioning jar 13, the stirring velocity of setting the first power spare 113 is 12r/min, and churning time is 36s;
First mixing component of startup stirring system stirs the mud of annotated sulfuric acid, ferric sulfate, flyash and concrete grey, and churning time is set at 40min, thereby, mud is nursed one's health;
After sludge conditioning finishes, will discharge from sludge out pipe 133 roads on the conditioning jar 13 through the mud of conditioning, so that follow-up further deep dehydration.
Below be example with the composite conditioner of bromine palm fibre trimethyl ammonium (CTAB) and flyash composition, the Opsonizing method of the automatic compound conditioning system 1 of sludge dewatering is described.
Deposit the pre-set programs that presets in the upper computer 101 in system 10, it can control the delivery rate of feeder 111 and the stirring velocity of stirring system etc.;
Through adding good certain density bromine palm fibre trimethyl ammonium (CTAB) solution of agent pipe 125 filling configured in advance in the liquid amendment jar 121, through hopper 112 flyash of in feeder 111, annotating;
Open Mud-intake valve door 138 and advance dredge pump 137; Make extraneous mud can enter into conditioning jars 13, after advancing mud and finishing, start first mixing component; This first mixing component stirs the mud in the conditioning jar 13, and the churning time speed setting is 300r/min;
The liquid amendment that starts in the second mixing component liquid towards amendment jar 121 carries out stir process, and stirring velocity is set at 100r/min, and churning time is set at 40min;
Start and advance agent valve 124 and agent-entering pump 123, make that the liquid amendment in the liquid amendment jar 121 is filled in the conditioning jar 13;
Start the first power spare 113, make that the solid-state amendment in the feeder 111 is filled in the conditioning jar 13, the velocity of rotation of the first power spare 113 is set at 24r/min, and rotation time is set at 16s;
First mixing component of startup stirring system stirs the mud of annotated bromine palm fibre trimethyl ammonium (CTAB) and flyash, and the setting churning time is 50min, thereby, mud is nursed one's health;
After sludge conditioning finishes, will discharge from sludge out pipe 133 roads on the conditioning jar 13 through the mud of conditioning, so that follow-up further deep dehydration.
The above is merely preferred embodiment of the present invention, not in order to restriction the present invention, all any modifications of within spirit of the present invention and principle, being done, is equal to and replaces and improvement etc., all should be included within protection scope of the present invention.
Claims (13)
1. the automatic compound conditioning system of sludge dewatering; It is characterized in that, comprise the mud that is used for holding the needs conditioning conditioning jar, several liquid amendment medicine systems, several solid-state amendment medicine systems, can the corresponding respectively said liquid amendment medicine system of control and said solid-state amendment medicine system drive the stirring system that the mud to said conditioning jar stirs and respectively the liquid amendment in said several liquid amendment medicine systems stirred to the system of said conditioning jar liquid amendment of compound filling and solid-state amendment and by said system.
2. the automatic compound conditioning system of sludge dewatering as claimed in claim 1 is characterized in that, also comprises detecting and to control the measuring element that said system starts to a said conditioning jar interior mud liquid level, and said measuring element is located at said conditioning jar.
3. according to claim 1 or claim 2 the automatic compound conditioning system of sludge dewatering; It is characterized in that; Said conditioning jar be provided with can supply mud get in the said conditioning jar advance the mud pipe and can supply to nurse one's health after mud discharge a said conditioning jar outer sludge out pipe; Saidly advance the mud pipe coupling dredge pump that advances by said system control operation is arranged; Its pipeline is provided with and can closes or open the said Mud-intake valve door that advances the mud pipe by the control of said system, and said sludge out pipe is connected with the shell pump by said system control operation, and its pipeline is provided with the mud extraction valve that can be closed or opened said sludge out pipe by said system control.
4. according to claim 1 or claim 2 the automatic compound conditioning system of sludge dewatering; It is characterized in that; But each said liquid amendment medicine system comprises and is used to hold the liquid amendment jar of liquid amendment, is communicated with said conditioning jar and said liquid amendment jar and feed flow attitude amendment respectively and gets into and advance the agent pipe in the said conditioning jar; And be communicated with said liquid amendment jar and can supply outside liquid amendment to get into and add the agent pipe in the said liquid amendment jar, the said pipeline that advances the agent pipe be provided with can by the agent-entering pump of said system control operation and can by said system control close or open said advance the agent pipe advance the agent valve.
5. according to claim 1 or claim 2 the automatic compound conditioning system of sludge dewatering; It is characterized in that each said solid-state amendment medicine system comprises the feeder that is communicated with said conditioning jar and is used to hold solid-state amendment, be communicated with said feeder and be used for the hopper of the solid-state amendment of filling in the said feeder and can be driven solid-state amendment filling to the said conditioning jar first interior power spare in the said feeder by said system.
6. according to claim 1 or claim 2 the automatic compound conditioning system of sludge dewatering; It is characterized in that said stirring system comprises and places in the said conditioning jar and can driven first mixing component that the mud in the said conditioning jar is stirred and placed in the said liquid amendment jar and can drive second mixing component that the liquid amendment in the said liquid amendment jar is stirred by said system by said system.
7. according to claim 1 or claim 2 the automatic compound conditioning system of sludge dewatering; It is characterized in that; Said system comprises the upper computer of the pre-set programs that can deposit external setting-up in and by the lower computer of said PC control, said lower computer is electrically connected at liquid amendment medicine system, solid-state amendment medicine system and stirring system respectively.
8. according to claim 1 or claim 2 the automatic compound conditioning system of sludge dewatering; It is characterized in that; Any one or a few of the SEPIGEL 305 that said liquid amendment is the solution form or sulfuric acid or ferric sulfate, said solid-state amendment are any one or a few of flyash or terra alba or cement of powder fine aggregate form.
9. the Opsonizing method of the automatic compound conditioning system of sludge dewatering is characterized in that,
The pre-set programs of external setting-up is deposited to system;
Annotate respectively in several liquid amendment medicine systems and several solid-state amendment medicine systems respectively liquid amendment and solid-state amendment;
Toward the conditioning jar mud that interior filling must be nursed one's health;
Said system starts stirring system to being opposite to said conditioning jar interior mud respectively and placing the liquid amendment in said several liquid amendment medicine systems to stir;
Said system is controlled said several liquid amendment medicine systems and said several solid-state amendment medicine systems liquid amendment of compound filling and solid-state amendment in the said conditioning jar respectively;
Said system starts said stirring system the mud of annotate liquid amendment and solid-state amendment is stirred;
The mud that stirs is discharged outside the said conditioning jar.
10. the Opsonizing method of the automatic compound conditioning system of sludge dewatering as claimed in claim 9; It is characterized in that: respectively in the said conditioning jar in the process of liquid amendment of compound filling and solid-state amendment, said system is controlled said liquid amendment medicine system and said solid-state amendment medicine system the annotate filling rate and the filling order of liquid amendment and solid-state amendment respectively in said several liquid amendment medicine systems and said several solid-state amendment medicine systems.
11. the Opsonizing method of the automatic compound conditioning system of sludge dewatering as claimed in claim 9 is characterized in that, after outside the said conditioning jar of the mud discharge that stirs, the automatic compound conditioning system of said sludge dewatering brings into operation again automatically.
12. Opsonizing method like claim 9 or the compound conditioning system of 10 or 11 described sludge dewaterings; It is characterized in that; Said stirring system is 100r/min~400r/min to the stirring velocity scope that the mud of the amendment of not annotating stirs, and the time range that the mud of filling amendment is stirred is 10min~60min.
13. Opsonizing method like claim 9 or the compound conditioning system of 10 or 11 described sludge dewaterings; It is characterized in that the stirring velocity scope that said stirring system is opposite to the liquid amendment in said several liquid amendment medicine systems is 50r/min~500r/min.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110455935.5A CN102531327B (en) | 2011-12-30 | 2011-12-30 | Sludge dewatering automatic combined cooker device and Opsonizing method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110455935.5A CN102531327B (en) | 2011-12-30 | 2011-12-30 | Sludge dewatering automatic combined cooker device and Opsonizing method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102531327A true CN102531327A (en) | 2012-07-04 |
CN102531327B CN102531327B (en) | 2016-08-17 |
Family
ID=46339543
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201110455935.5A Active CN102531327B (en) | 2011-12-30 | 2011-12-30 | Sludge dewatering automatic combined cooker device and Opsonizing method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102531327B (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103193374A (en) * | 2013-05-03 | 2013-07-10 | 湖南品铸科技发展有限公司 | Sludge dewatering tempering agent and method for sludge dewatering by utilizing same |
CN103241921A (en) * | 2012-08-07 | 2013-08-14 | 江苏绿威环保科技有限公司 | Intelligent conditioning system for deep dewatering of sludge |
CN104692611A (en) * | 2015-02-15 | 2015-06-10 | 南京中衡元环保设备有限公司 | Waste catalyst mud water dehydration treatment equipment and waste catalyst mud water dehydration treatment method |
CN106396316A (en) * | 2016-12-05 | 2017-02-15 | 上海申耀环保工程有限公司 | Sludge curing agent as well as preparation method and use method thereof |
CN110255857A (en) * | 2019-05-28 | 2019-09-20 | 路德环境科技股份有限公司 | Low alkali conditioner and dewatering for construction slurry deep dehydration |
CN112010532A (en) * | 2020-09-16 | 2020-12-01 | 北京城市排水集团有限责任公司清河第二再生水厂 | Sludge treatment system and sludge treatment method |
CN114436498A (en) * | 2022-02-07 | 2022-05-06 | 广州绿邦环境技术有限公司 | Sludge conditioning device and treatment process thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201825835U (en) * | 2010-11-01 | 2011-05-11 | 宇星科技发展(深圳)有限公司 | Novel sludge conditioning device |
CN202499798U (en) * | 2011-12-30 | 2012-10-24 | 宇星科技发展(深圳)有限公司 | Sludge dewatering automatic composite conditioning device |
-
2011
- 2011-12-30 CN CN201110455935.5A patent/CN102531327B/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201825835U (en) * | 2010-11-01 | 2011-05-11 | 宇星科技发展(深圳)有限公司 | Novel sludge conditioning device |
CN202499798U (en) * | 2011-12-30 | 2012-10-24 | 宇星科技发展(深圳)有限公司 | Sludge dewatering automatic composite conditioning device |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103241921A (en) * | 2012-08-07 | 2013-08-14 | 江苏绿威环保科技有限公司 | Intelligent conditioning system for deep dewatering of sludge |
CN103241918A (en) * | 2012-08-07 | 2013-08-14 | 江苏绿威环保科技有限公司 | Intelligent conditioning system for deep dewatering of sludge |
CN103241918B (en) * | 2012-08-07 | 2015-01-21 | 江苏绿威环保科技有限公司 | Intelligent conditioning system for deep dewatering of sludge |
CN103241921B (en) * | 2012-08-07 | 2015-03-25 | 江苏绿威环保科技有限公司 | Intelligent conditioning system for deep dewatering of sludge |
CN103193374A (en) * | 2013-05-03 | 2013-07-10 | 湖南品铸科技发展有限公司 | Sludge dewatering tempering agent and method for sludge dewatering by utilizing same |
CN104692611A (en) * | 2015-02-15 | 2015-06-10 | 南京中衡元环保设备有限公司 | Waste catalyst mud water dehydration treatment equipment and waste catalyst mud water dehydration treatment method |
CN106396316A (en) * | 2016-12-05 | 2017-02-15 | 上海申耀环保工程有限公司 | Sludge curing agent as well as preparation method and use method thereof |
CN110255857A (en) * | 2019-05-28 | 2019-09-20 | 路德环境科技股份有限公司 | Low alkali conditioner and dewatering for construction slurry deep dehydration |
CN110255857B (en) * | 2019-05-28 | 2021-12-14 | 路德环境科技股份有限公司 | Low-alkali conditioner for deep dehydration of building slurry and dehydration method |
CN112010532A (en) * | 2020-09-16 | 2020-12-01 | 北京城市排水集团有限责任公司清河第二再生水厂 | Sludge treatment system and sludge treatment method |
CN114436498A (en) * | 2022-02-07 | 2022-05-06 | 广州绿邦环境技术有限公司 | Sludge conditioning device and treatment process thereof |
CN114436498B (en) * | 2022-02-07 | 2024-03-26 | 广州绿邦环境技术有限公司 | Sludge conditioning device and treatment process thereof |
Also Published As
Publication number | Publication date |
---|---|
CN102531327B (en) | 2016-08-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102531327A (en) | Automatic compound conditioning device and conditioning method for sludge dewatering | |
CN109133553A (en) | A kind of continous way sludge conditioning system and its apparatus | |
CN102452775A (en) | Novel sludge conditioning device and conditioning method | |
CN206266295U (en) | Medicine system and sewage disposal system | |
CN105019195A (en) | Powder feeding and dissolving device and washing machine | |
CN203803394U (en) | Automatic medicine dissolving device | |
CN102580363A (en) | Device for adding flocculant | |
CN202499798U (en) | Sludge dewatering automatic composite conditioning device | |
CN102849837A (en) | Chemicals feeding device | |
CN203061130U (en) | Flocculant stirring device | |
CN206173067U (en) | Abandonment drilling fluid flocculation dewatering device | |
CN212198638U (en) | Dosing device in ammonium phosphate coolant liquid recovery treatment system | |
CN204275824U (en) | Three groove continous way drug delivery dissolvers | |
CN208414264U (en) | A kind of processing system of vacuum salt production by-produced gypsum | |
CN201825835U (en) | Novel sludge conditioning device | |
CN103896475A (en) | Regulation method for high-dryness dehydration of sludge | |
CN210999406U (en) | Device is used in modified phosphogypsum production | |
JP3231501U (en) | Triplet supply, dissolution and dosing equipment for bottom mud dewatering in river ecological sludge treatment | |
CN212396611U (en) | Automatic flocculating agent diluting and adding device | |
CN202849134U (en) | Chemical dosing device | |
CN215828615U (en) | Automatic dosing device for sludge dewatering | |
CN206027600U (en) | Special treatment device for waste drilling fluid rubber crushing and mixing | |
CN206244634U (en) | Dosing is dehydrated abatement system | |
CN201981026U (en) | Automatic medicament dissolving and adding device | |
CN111389853A (en) | Earth pressure balance shield mud curing treatment system |
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 |