CN104399381A - SAN continuous dye configuration device and configuration method - Google Patents

SAN continuous dye configuration device and configuration method Download PDF

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Publication number
CN104399381A
CN104399381A CN201410456780.0A CN201410456780A CN104399381A CN 104399381 A CN104399381 A CN 104399381A CN 201410456780 A CN201410456780 A CN 201410456780A CN 104399381 A CN104399381 A CN 104399381A
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CN
China
Prior art keywords
san
dye
configuration
tank
mother liquor
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.)
Pending
Application number
CN201410456780.0A
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Chinese (zh)
Inventor
陈伟峰
刘格宏
安明海
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DAJIE CHEMICAL Co Ltd TIANJIN
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DAJIE CHEMICAL Co Ltd TIANJIN
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by DAJIE CHEMICAL Co Ltd TIANJIN filed Critical DAJIE CHEMICAL Co Ltd TIANJIN
Priority to CN201410456780.0A priority Critical patent/CN104399381A/en
Publication of CN104399381A publication Critical patent/CN104399381A/en
Pending legal-status Critical Current

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Abstract

A SAN continuous dye configuration device and a configuration method are disclosed. The configuration device comprises a SAN unit composed of two configuration tanks with stirrers and three vertical diaphragm metering pumps. Two filters are connected in parallel between the two configuration tanks and the three diaphragm metering pumps. The two configuration tanks are connected in parallel with the three diaphragm metering pumps. The configuration method comprises the following steps: firstly, a powdery dye is dissolved in styrene to prepare a mother liquor of the dye; secondly, the mother liquor of the dye is added into a stirring pot A through a charging pipe nipple, and a lot of styrene is added into the stirring pot and stirring is carried out to prepare a blue SAN dyeing liquor; thirdly, stirring starts to uniformly mix the blue dye; and finally, the vertical diaphragm metering pumps are started, and the dye in the pot is pumped to the next production process so as to complete configuration of the SAN unit. The invention has the following beneficial effect: the continuous dye device has advantages of high reliability, large handling capacity, low labor cost, low energy consumption, good product quality and excellent dyeing effect.

Description

SAN continuous dye inking device and collocation method thereof
Technical field
The present invention relates to a kind of Chemical Manufacture automatics, particularly relate to SAN continuous dye inking device and collocation method.
Background technology
The solid particles of normal SAN particle to be a kind of be light, but fewer and feweri to the demand of common SAN particle on market in recent years, to the demand showed increased of dyeing SAN particle (mainly blue).In order to produce blue SAN particle, this just needs to add certain stains in course of reaction, needs to add dyestuff feeding line in raw material pan feeding, and arranges dyestuff material-compound tank.
Summary of the invention
The object of this invention is to provide a kind of SAN continuous dye dispenser, provide a kind of collocation method reliability high simultaneously, treating capacity is large, and labour cost is few, and energy consumption is low.
In order to achieve the above object, the technical solution used in the present invention is:
A kind of SAN continuous dye inking device, it is characterized in that: comprise the SAN unit be made up of the preparing tank of two subsidiary stirrings and three vertical diaphragm measuring pumps, between two preparing tanks and three measuring pumps, be connected in parallel two filters, two described preparing tanks and three measuring pumps are for being connected in parallel.
A kind of SAN continuous dye collocation method, is characterized in that: comprise the following steps, is first dissolved in styrene by pulverous dyestuff, be mixed with the mother liquor of dyestuff; Joined in agitator tank A by reinforced pipe nipple, add the dyeing liquor that a large amount of styrene is configured to blue SAN again in agitator tank; Start and stir, blue dyes is mixed; Start vertical metering diaphragm pump, the dyestuff in tank is got in next production process, complete SAN cell location.
In above-described step, the time of staying of SAN cell location is 3 hours.
In above-described step, styrene is transported in preparing tank A, adds anthraquinone dyes, use batch tank A to stir to stir mother liquor, in whipping process, by filter A, enter into the import of measuring pump A, be transported in next production process by measuring pump; When the mother liquor of preparing tank A is soon finished, use same step, in preparing tank B, configure mother liquor, use preparing tank B to stir; When filter A blocks, be switched to filter B; When measuring pump A goes wrong, measuring pump B or measuring pump C can be switched, carry out continuous seepage.
Beneficial aspects of the present invention is: continuous dye device, and reliability is high, and treating capacity is large, and labour cost is few, and energy consumption is low, good product quality, and Color is good.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
In figure: 1. preparing tank A stirs; 2. preparing tank A; 3 preparing tank B stir; 4. preparing tank B; 5. filter A; 6. filter B; 7. measuring pump A; 8. measuring pump B; 9. measuring pump C.
Detailed description of the invention
As shown in Figure 1, the present invention includes the SAN unit be made up of two subsidiary preparing tank 1,2 and three vertical diaphragm measuring pumps 7,8,9 stirred, between two preparing tanks and three measuring pumps, be connected in parallel two filters 5,6, two described preparing tanks and three measuring pumps are for being connected in parallel.Styrene is transported in preparing tank A 2, adds anthraquinone dyes, use batch tank A to stir 1 pair of mother liquor and stir, in whipping process, by filter A5, enter into the import of measuring pump A7, be transported in next production process reactor (not shown) by measuring pump.When the mother liquor of preparing tank A2 is soon finished, use same step, in preparing tank B4, configure mother liquor, use preparing tank B to stir 3 and stir.When filter A5 blocks, be switched to filter B 6.When measuring pump A7 goes wrong, measuring pump B8 or measuring pump C9 can be switched, carry out continuous seepage, realize continuous automatic operation.
The time of staying of SAN unit is 3 hours, after blue dyes charging, can find out that from granulating system and blast system presenting of SAN particle is blue after 3 hours, by the aberration of testing SA N particle, monitor its stability and blue degree, and according to the blue degree of depth of customer requirement, can adjust blue mother liquid concentration to change the blue depth of final blue SAN particle.

Claims (4)

1. a SAN continuous dye inking device, it is characterized in that: comprise the SAN unit be made up of the preparing tank of two subsidiary stirrings and three vertical diaphragm measuring pumps, between two preparing tanks and three measuring pumps, be connected in parallel two filters, two described preparing tanks and three measuring pumps are for being connected in parallel.
2. a SAN continuous dye collocation method, is characterized in that: comprise the following steps, and is first dissolved in styrene by pulverous dyestuff, is mixed with the mother liquor of dyestuff; Joined in agitator tank A by reinforced pipe nipple, add the dyeing liquor that a large amount of styrene is configured to blue SAN again in agitator tank; Start and stir, blue dyes is mixed; Start vertical metering diaphragm pump, the dyestuff in tank is got in next production process, complete SAN cell location.
3. method according to claim 2, is characterized in that: in above-described step, and the time of staying of SAN cell location is 3 hours.
4. method according to claim 2, it is characterized in that: in above-described step, styrene is transported in preparing tank A, add anthraquinone dyes, use batch tank A to stir to stir mother liquor, in whipping process, by filter A, enter into the import of measuring pump A, be transported in next production process by measuring pump; When the mother liquor of preparing tank A is soon finished, use same step, in preparing tank B, configure mother liquor, use preparing tank B to stir; When filter A blocks, be switched to filter B; When measuring pump A goes wrong, measuring pump B or measuring pump C can be switched, carry out continuous seepage.
CN201410456780.0A 2014-09-10 2014-09-10 SAN continuous dye configuration device and configuration method Pending CN104399381A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410456780.0A CN104399381A (en) 2014-09-10 2014-09-10 SAN continuous dye configuration device and configuration method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410456780.0A CN104399381A (en) 2014-09-10 2014-09-10 SAN continuous dye configuration device and configuration method

Publications (1)

Publication Number Publication Date
CN104399381A true CN104399381A (en) 2015-03-11

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CN201410456780.0A Pending CN104399381A (en) 2014-09-10 2014-09-10 SAN continuous dye configuration device and configuration method

Country Status (1)

Country Link
CN (1) CN104399381A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2017910A1 (en) * 1968-09-12 1970-05-22 Orlita Franz
US20010048637A1 (en) * 2000-05-24 2001-12-06 Weigl Bernhard H. Microfluidic system and method
JP2008069325A (en) * 2006-09-15 2008-03-27 Fujifilm Corp Pigment dispersion composition
CN203159569U (en) * 2013-02-06 2013-08-28 深圳市长隆能源股份有限公司 Automatic liquid catalyst proportioning and conveying device
CN203370498U (en) * 2013-07-11 2014-01-01 浙江东发环保工程有限公司 Automatic preparing and adding device of liquid preparations

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2017910A1 (en) * 1968-09-12 1970-05-22 Orlita Franz
US20010048637A1 (en) * 2000-05-24 2001-12-06 Weigl Bernhard H. Microfluidic system and method
JP2008069325A (en) * 2006-09-15 2008-03-27 Fujifilm Corp Pigment dispersion composition
CN203159569U (en) * 2013-02-06 2013-08-28 深圳市长隆能源股份有限公司 Automatic liquid catalyst proportioning and conveying device
CN203370498U (en) * 2013-07-11 2014-01-01 浙江东发环保工程有限公司 Automatic preparing and adding device of liquid preparations

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
卓昌明主编: "《塑料应用技术手册》", 31 May 2013, 机械工业出版社 *
席建荣,张守汉: "浅紫罗兰色苯乙烯一丙烯腈共聚物树脂的工业开发", 《石化技术与应用》 *

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Application publication date: 20150311