CN204583103U - The adding set of 4A zeolite in a kind of non-phosphide detergent production process - Google Patents
The adding set of 4A zeolite in a kind of non-phosphide detergent production process Download PDFInfo
- Publication number
- CN204583103U CN204583103U CN201520183596.3U CN201520183596U CN204583103U CN 204583103 U CN204583103 U CN 204583103U CN 201520183596 U CN201520183596 U CN 201520183596U CN 204583103 U CN204583103 U CN 204583103U
- Authority
- CN
- China
- Prior art keywords
- crystallization groove
- zeolite
- dissolving tank
- feeding pipe
- communicated
- 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 - Fee Related
Links
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Detergent Compositions (AREA)
Abstract
The utility model relates to the adding set of 4A zeolite in a kind of non-phosphide detergent production process, belong to non-phosphide detergent process units technical field, it comprises the first dissolving tank for generating sodium aluminate, for the second dissolving tank of stirring and dissolving waterglass and crystallization groove; Described first dissolving tank is communicated with crystallization groove by feeding pipe, described second dissolving tank is communicated with crystallization groove by feeding pipe, described crystallization groove is communicated with dosage bunker by feeding pipe, described crystallization groove is provided with the jet chimney for passing into steam in crystallization groove.This device adds 4A zeolite slurry in the process of producing washing powder, eliminate the filtration of 4A zeolite slurry, washing, spraying dry and packaging supervisor, save operation and time, and the alkali that well make use of in 4A zeolite slurry and moisture, reduce production cost.
Description
Technical field
The utility model relates to the device producing non-phosphide detergent with 4A zeolite, is specially the adding set of 4A zeolite in a kind of non-phosphide detergent production process.
Background technology
Current industrial production non-phosphide detergent needs to add following raw material: detergent, 4A zeolite and alkali; Above-mentioned raw materials fully mixes and spray-dried final obtained finished product in aqueous.Wherein 4A zeolite is used for soft water auxiliary agent, is also used as adsorbent, dehydrating agent and catalyst.During alkali is used for and acid detergent, regulate pH.
Because product needed is spray-dried rear obtained, therefore when producing, often adding pulverous 4A zeolite and bringing unnecessary moisture into reduce.Chinese patent CN103865678A discloses and a kind of in detergent raw material, to add after the mixing of 4A zeolite powder spray-dired method again, but like this 4A zeolite in process of production first after batch mixing pulp, crystallization spraying dry be prepared as powder, later stage is mixed into detergent raw material (wet feed), row spraying dry again after mixing, cause the waste in operation, and the water yield used when preparing 4A zeolite, cannot use, also result in the waste of water resource in subsequent handling.Disclose the technique that 4A zeolite powder and other washing powder powder are directly mixed with washing powder in cylinder in patent CN103113996A, but owing to using powder, one is not easily mix, increases labour intensity; Two is easily cause dust pollution, and harm operator is healthy.
Utility model content
Technical problem to be solved in the utility model is to provide the adding set of 4A zeolite in a kind of non-phosphide detergent production process, and it can simplify production technology, reduce production cost.
The utility model adopts following technical scheme:
An adding set for 4A zeolite in non-phosphide detergent production process, its key technology is: it comprises for stirring and dissolving Al (OH)
3with with first dissolving tank of NaOH, for the second dissolving tank of stirring and dissolving waterglass and crystallization groove; Described first dissolving tank is communicated with crystallization groove by feeding pipe, and described second dissolving tank is communicated with crystallization groove by feeding pipe, and described crystallization groove is communicated with dosage bunker by feeding pipe, described feeding pipe is provided with valve and mashing pump; Described crystallization groove is provided with the jet chimney for passing into steam in crystallization groove.
Good effect of the present utility model is as follows:
Technical scheme disclosed in the utility model, has abandoned the outmoded way in conventional production equipment and production process, will dissolve Al (OH)
3be communicated with crystallization groove by feeding pipe with the second dissolving tank of dissolved water glass with first dissolving tank of NaOH simultaneously, to crystallization groove supply material, Al (OH) in the first dissolving tank
3stir and evenly mix in crystallization groove with waterglass after generating sodium aluminate with NaOH solution, pass in whipping process after steam makes material pulp, crystallization and obtain 4A zeolite slurry, then direct 4A zeolite slurry is driven in dosage bunker by feeding pipe, coordinate after stirring with detergent raw material, by feeding pipe, material is passed in spray dryer, both obtained washing powder.
This device adds 4A zeolite slurry in the process of producing washing powder, eliminates the spraying dry program of 4A zeolite slurry, saves operation and time, and well make use of the moisture in 4A zeolite slurry, saves raw material, reduces production cost.
The utility model changes the method that existing non-phosphide detergent adds 4A zeolite, directly adds 4A zeolite with slip form.The method small investment, instant effect, cost are low, greatly can reduce the production cost of non-phosphide detergent.Meanwhile, reduce the labour intensity adding phosphorus-free adjuvant 4A zeolite in non-phosphide detergent production process, avoid the dust pollution in existing oven dry 4A zeolite product adding procedure, thus reach energy-saving and cost-reducing, the object of cost efficiency.
Accompanying drawing explanation
Accompanying drawing 1 is the utility model structural representation.
In the accompanying drawings: 10 first dissolving tanks, 20 second dissolving tanks, 30 crystallization grooves, 40 dosage bunkers, 50 spray dryers; 01 valve, 02 mashing pump, 03 feeding pipe, 04 jet chimney.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
The adding set of 4A zeolite in a kind of non-phosphide detergent production process as shown in Figure 1, it comprises for stirring and dissolving Al (OH)
3with first dissolving tank 10 of NaOH, for the second dissolving tank 20 of stirring and dissolving waterglass and crystallization groove 30; The first described dissolving tank 10 is for stirring and dissolving Al (OH)
3production sodium aluminate is made with NaOH.The first described dissolving tank 10 and the second dissolving tank 20 can be also reactor, are wherein provided with paddle, can be anchor formula stirring arm, frame type agitating blade or Combined stirring paddle.Described crystallization groove 30 also can be reactor.
Described first dissolving tank 10 is communicated with crystallization groove 30 by feeding pipe 03, described second dissolving tank 20 is communicated with crystallization groove 30 by feeding pipe 03, described crystallization groove 30 is communicated with dosage bunker 40 by feeding pipe 03, described feeding pipe 03 is provided with valve 01 and mashing pump 02; Described crystallization groove 30 is provided with the jet chimney 04 for passing into steam in crystallization groove 30.
The discharging opening of described first dissolving tank 10, second dissolving tank 20 and crystallization groove 30 is all arranged on bottom, and bottom is taper or standard elliptical head, and material can be made to discharge completely, and internal tank is airtight, can pass into the transfer that compressed air or nitrogen supercharging carry out material.The present embodiment adopts mashing pump 02 to carry out providing power to material transfer.
Described dosage bunker 40 is communicated with spray dryer 50 by conveyance conduit 03, described conveyance conduit 03 is arranged valve 01 and mashing pump 02.Al (OH) will be dissolved
3be communicated with crystallization groove 30 by feeding pipe 03 with the second dissolving tank 20 of dissolved water glass with first dissolving tank 10 of NaOH simultaneously, supply material to crystallization groove 30, Al (OH) in the first dissolving tank 10
3stir and evenly mix in crystallization groove 30 with waterglass after generating sodium aluminate with NaOH solution, passed into after steam makes material pulp, crystallization by jet chimney 04 in whipping process and obtain 4A zeolite slurry, then direct 4A zeolite slurry is driven in dosage bunker 40 by feeding pipe 03, after in dosage bunker 40,4A zeolite slurry coordinates with detergent raw material and stirs, by feeding pipe 03, material is passed in spray dryer 50, both obtained washing powder.
Last it is noted that above embodiment is only in order to illustrate the technical solution of the utility model, be not intended to limit; Although be described in detail the utility model with reference to previous embodiment, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in previous embodiment, or carries out equivalent replacement to wherein portion of techniques feature; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of the utility model embodiment technical scheme.
Claims (1)
1. the adding set of 4A zeolite in non-phosphide detergent production process, is characterized in that: it comprises for stirring and dissolving Al (OH)
3with first dissolving tank (10) of NaOH, for second dissolving tank (20) of stirring and dissolving waterglass and crystallization groove (30);
Described first dissolving tank (10) is communicated with crystallization groove (30) by feeding pipe (03), described second dissolving tank (20) is communicated with crystallization groove (30) by feeding pipe (03), described crystallization groove (30) is communicated with dosage bunker (40) by feeding pipe (03), described feeding pipe (03) is provided with valve (01) and mashing pump (02);
Described crystallization groove (30) is provided with the jet chimney (04) for passing into steam in crystallization groove (30).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520183596.3U CN204583103U (en) | 2015-03-30 | 2015-03-30 | The adding set of 4A zeolite in a kind of non-phosphide detergent production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520183596.3U CN204583103U (en) | 2015-03-30 | 2015-03-30 | The adding set of 4A zeolite in a kind of non-phosphide detergent production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204583103U true CN204583103U (en) | 2015-08-26 |
Family
ID=53919304
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520183596.3U Expired - Fee Related CN204583103U (en) | 2015-03-30 | 2015-03-30 | The adding set of 4A zeolite in a kind of non-phosphide detergent production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204583103U (en) |
-
2015
- 2015-03-30 CN CN201520183596.3U patent/CN204583103U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102515610B (en) | Aliphatic series high efficiency water reducing agent and preparation method thereof | |
| CN101993085B (en) | Method for producing white carbon black for toothpaste from fly ash | |
| CN204583103U (en) | The adding set of 4A zeolite in a kind of non-phosphide detergent production process | |
| CN105839188A (en) | Method of producing calcium silicate crystal whiskers with fly ash desilication liquid | |
| CN203955215U (en) | A kind of Anti-caking rabbling mechanism of glassed steel reaction vessels | |
| CN201712064U (en) | Device for adding liquid polycarboxylic acid water reducing agent into dry powder mortar | |
| CN104556056B (en) | Utilize the method for high silica flour coal ash production of silica white | |
| CN206483477U (en) | A kind of industrial chemicals extraction element | |
| CN102337690B (en) | Pulping method for stewing bamboo material by using aluminum salt and retaining silicon at same time | |
| CN201545709U (en) | Device for producing feed grade one-hydrate ferrous sulfate | |
| CN204819911U (en) | Dry process gypsum block production line | |
| CN204529341U (en) | A kind of oxidation reaction apparatus preparing red iron oxide | |
| CN206654742U (en) | A kind of active nano-calcium carbonate is prepared with carbonization coating equipment | |
| CN107311136B (en) | Method and device for producing granular sodium tripolyphosphate | |
| CN107416874B (en) | A kind of dealkalization method of coal ash lifting aluminium slag | |
| CN205473484U (en) | Raw material feed device of nitromethane building -up reactions | |
| CN204997816U (en) | A novel single horizontal axis mixer for concrete preparation | |
| CN111068562A (en) | Production method of high-protein-content gunite corn husks | |
| CN202638431U (en) | Efficient and energy-saving type carbonization reaction device | |
| CN202730524U (en) | Non-pulping continuous cleaning device for purified cotton pulp | |
| CN112028084B (en) | Method and equipment for preparing borax | |
| CN205269477U (en) | Mixing stirring device that tombarthite phosphor powder waste material was used | |
| CN201574125U (en) | Production equipment for naphthalene sulfonate water-reducing admixture | |
| CN213699347U (en) | Pollution-free treatment structure for water glass waste gas | |
| CN219784220U (en) | Calcium carbonate carbonization tower internal circulation spray reaction dust collecting equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20170710 Granted publication date: 20150826 |
|
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20180710 Granted publication date: 20150826 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150826 Termination date: 20170330 |