CN105481136B - The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production - Google Patents

The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production Download PDF

Info

Publication number
CN105481136B
CN105481136B CN201510840391.2A CN201510840391A CN105481136B CN 105481136 B CN105481136 B CN 105481136B CN 201510840391 A CN201510840391 A CN 201510840391A CN 105481136 B CN105481136 B CN 105481136B
Authority
CN
China
Prior art keywords
water
waste
algin
calcium
integrated conduct
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.)
Active
Application number
CN201510840391.2A
Other languages
Chinese (zh)
Other versions
CN105481136A (en
Inventor
惠锋基
林成彬
王斌
滕怀华
韦晓廷
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.)
SHANDONG JIEJING GROUP Corp
Original Assignee
SHANDONG JIEJING GROUP Corp
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.)
Filing date
Publication date
Application filed by SHANDONG JIEJING GROUP Corp filed Critical SHANDONG JIEJING GROUP Corp
Priority to CN201510840391.2A priority Critical patent/CN105481136B/en
Publication of CN105481136A publication Critical patent/CN105481136A/en
Application granted granted Critical
Publication of CN105481136B publication Critical patent/CN105481136B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention belongs to the technical field of seaweed chemical production, is specifically related to the integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production.This kind of integrated conduct method, comprises the following steps:(1)Suspension in waste Ca water is removed;(2)Decalcifying agent is added in waste Ca water and carries out decalcification processing, is then settled;(3)Recycle-water is directly used as after the removal of impurities of gained supernatant is handled;Calcium carbonate is added into waste acid water, reaction obtains calcium chloride solution, and hydrochloric acid is then added in calcium chloride solution causes calcium chloride mass concentration to be at least up to 12%;(4)After calcium chloride solution is filtered, glue calcification process in algin production is directly used in.The technique, which overcomes, settles the shortcomings of difficult, cost is high, generation a large amount of calcium salt discarded objects in wastewater treatment, realize the comprehensive cyclic utilization of algin processing waste water.

Description

The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production
Technical field
The invention belongs to the technical field of seaweed chemical production, is specifically related to waste Ca water in a kind of algin production and gives up The integrated conduct method that sour water recycles.
Background technology
In seaweed chemical industry, with the algin of brown alga production(Also known as sodium alginate, sodium alginate), its production technology Existing more than 40 years history, has been widely used for the multiple fields such as food, weaving, printing and dyeing, chemical industry, medicine, agricultural, demand at present Measure increasing.The production of present China algin, it is largely to use calcification, acidization, often produces one ton of product water consumption and exist 600-800 tons, except produce more than 100 tons immersion edible seaweed high-concentration waste water, more than 20 ton pH value outside 1.5 or so waste acid water, its Remaining is waste Ca water of the hardness in German degree 50-90, and these waste water directly discharge after COD drops in sewage disposal at present, cause Can a large amount of wastes of water resource, especially current freshwater resources be increasingly reduced, reduce water consume and accomplish that cleanly production turns into brown The key of phycocolloid industry future survival and development.
Caused waste Ca water and waste acid water in algin production, calcium ion content is high and contains a small amount of low molecule algin, Waste acid water pH value 1.5 or so, it is relatively difficult into environment friendly system processing, but it is not other in addition to containing above-mentioned substance in waste water Impurity.
It is existing at present to there is chemical precipitation method, hyperfiltration, electroosmose process, resin ion to hand over for waste Ca water handling process Method etc. is changed, wherein " wastewater recycling method in a kind of seaweed chemical production " open one kind uses chemical precipitation method by waste water Again by the method for the further reuse of technique waste water after middle calcium ion removal;" the double alkali of calcic waste water sink in processing brown alga chemical industry Shallow lake method " is disclosed the method for the further reuse of technique waste water after a kind of double alkaline precipitations of use remove calcium ion in waste water;It is " brown The open one kind of the process of processing and the circulating and recovering zero-emission of phycocolloid production waste water " is given up using reverse osmosis technology handling process Water and then the further method of reuse;The patent of invention of " a kind of New process for comprehensively utilizing brown alga chemical calcium wastewater " discloses one Kind electrodialysis and resin cation handling process method.
Following defect be present in existing waste Ca water processing method:(1)The recycle-water for being used as flocculant process with aluminum oxide can not Produced in foodstuff glue;(2)The pure chemistry precipitation method, 4-5 hours or overnight need to be stood during processing, time oversize unsuitable industrialization Commercial cultivation;(3)Counter-infiltration, electrodialysis, resin method processing cost are too high, add product cost, it is competing to reduce enterprise product Strive power.
The content of the invention
It is an object of the invention to not thorough, the increasing for caused waste Ca water and spent acid water process in the production of current algin The problem of cannot effectively being utilized after the stress problems of big follow-up environmental protection treatment, and processing and provide in a kind of algin production The integrated conduct method of waste Ca water and spent acid water circulation use.Integrated conduct method of the present invention is in treatment for reuse waste Ca water And while waste acid water, can reach the output object comprehensive utilization in processing procedure, technique overcome settled in wastewater treatment it is difficult, into This height, the shortcomings of a large amount of calcium salt discarded objects is produced, realize the comprehensive cyclic utilization of algin processing waste water.
The technical scheme is that:The integrated treatment side of waste Ca water and spent acid water circulation use in a kind of algin production Method, comprise the following steps:(1)Suspension containing low molecule calcium alginate in waste Ca water is removed;(2)By step(1) Decalcifying agent is added in waste Ca water after processing and carries out decalcification processing, is then settled, obtains supernatant and sediment calcium carbonate; (3)Gained supernatant is first passed through to the recycle-water for being directly used as that latting drown process is digested in algin production after removal of impurities is handled;By institute Obtain sediment calcium carbonate to add into waste acid water after collection, reaction obtains calcium chloride solution, then molten in the calcium chloride of gained Hydrochloric acid is added in liquid causes calcium chloride mass concentration to be at least up to 12%;(4)Gained mass concentration is at least to 12% calcium chloride After solution is filtered, glue calcification process in algin production is directly used in.
The step(1)The suspension containing low molecule calcium alginate in waste Ca water is gone using air floatation machine or centrifuge Remove.
The step(2)Middle decalcifying agent is sodium carbonate.
The step(2)The addition of middle decalcifying agent is 1~1.2 times of calcium ion mole in waste Ca water.
The step(2)Middle sedimentation uses standing sedimentation 0.5~1 hour.
The step(2)Middle sedimentation carries out continuous sedimentation using inclined plate sedimentation pond.
The step(3)Middle supernatant carries out removal of impurities processing by 300 mesh net filtrations or centrifuge.
The step(3)The salt content of middle recycle-water is less than or equal to 3%.
The step(4)The calcium chloride solution that middle mass concentration is at least 12% is filtered by 300 mesh nets.
Beneficial effects of the present invention are:The synthesis of waste Ca water and spent acid water circulation use in algin production of the present invention Waste Ca water Treatment for Reuse removes the suspensions such as a small amount of calcium alginate in waste Ca water using Bubble-floating Method or centrifugal process in processing method, The factor for calcium carbonate sinking speed of eliminating the effects of the act, using chemical reagent sedimentation, by 1-1.2 times of mol ratio of calcium ion to waste Ca water Middle addition decalcifying agent, waste Ca water hardness is handled to German degree below 5, supernatant is filtered or centrifugation direct reuse is in algin Production digestion latting drown process.Waste Ca water reprocessing is no more than 3% using to salt content;The Treatment for Reuse of waste acid water, above-mentioned processing Sediment afterwards, reacts with waste acid water to obtain calcium chloride solution after collection, and concentrated hydrochloric acid is added in above-mentioned processing makes gained chlorine Change calcium concentration and reach more than 12%, the calcification process of algin production is directly used in after filtering.Treatment for reuse waste Ca water of the present invention and While waste acid water, the output object comprehensive utilization in processing procedure is can reach, technique, which overcomes, settles difficult, cost in wastewater treatment Height, the shortcomings of a large amount of calcium salt discarded objects is produced, realize the comprehensive cyclic utilization of algin processing waste water.
The integrated conduct method of waste Ca water and spent acid water circulation use causes in waste Ca water not only in the algin production Do not contain calcium ion while be free of low molecule algin, waste acid water has been fully processed, and environment friendly system processing is tired in the absence of entering The problem of difficult.The integrated conduct method makes the Ca in algin production2+And H+Reach complete recycling, greatly reduce brown alga Glue workshop cost.The recycle-water salt content after as long as lot of experiments finds processing, completely can be by after its decalcification below 3% Reuse does not influence into technique on production technology and product quality, can greatly reduce the industrial water amount of algin;And locate Calcium carbonate caused by waste Ca water and waste acid water reaction generation calcium chloride are managed, calcification process can be back to use, not only make use of processing Calcium carbonate solid waste caused by water, the problem of also solving spent acid water process difficulty, add recycling for various raw material Rate, the comprehensive utilization of waste is realized, reduce production cost while having saved with water, reduce environmental pollution.
In summary, recycle-water is caused to can be used for foodstuff glue production using processing method of the present invention;Processing time It is short, it is adapted to industrialized production to utilize;Processing cost is low, and then reduces the production cost of product.
Embodiment
Below by embodiment, the present invention will be described in detail.
Embodiment 1
The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production, comprises the following steps:(1) Removed, obtained clear by the suspension containing low molecule calcium alginate is derived from the 10L waste Ca waters in algin workshop using centrifuge Clear liquid body;Wherein the German degree of waste Ca water is 55, salt content 0.32%;(2)By step(1)In waste Ca water after processing The sodium carbonate 10.41g for adding 1 times of calcium ion mole carries out decalcification processing.Then settled, it is small using standing sedimentation 1 When, obtain supernatant and sediment calcium carbonate;(3)Gained supernatant is first passed through into 300 mesh net filtrations or centrifuge is carried out Removal of impurities is handled;It is directly used as digesting the recycle-water of latting drown process, wherein recycle-water after removal of impurities is handled in algin production Salt content is 0.33%, and German degree is 4.6.Gained sediment calcium carbonate is added to the 40ml waste acid waters that pH is 1.6 after collection In, 30% hydrochloric acid 30ml is added, calcium carbonate is stirred well to and reacts completely, it is 12.5% calcium chloride solution that reaction, which obtains concentration, Then hydrochloric acid is added in the calcium chloride solution of gained causes calcium chloride mass concentration to be at least up to 12%;(4)Gained quality is dense After the calcium chloride solution spent for 12.5% is filtered by 300 mesh nets, glue calcification process in algin production is directly used in.
Embodiment 2
The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production, comprises the following steps:(1) Removed, obtained by the suspension containing low molecule calcium alginate is derived from the 500L waste Ca waters in algin workshop using air soluble method air supporting To supernatant liquid;Wherein the German degree of waste Ca water is 68, salt content 0.45%;(2)By step(1)Useless calcium after processing The sodium carbonate 708g that 1.1 times of calcium ion moles are added in water carries out decalcification processing.Then settled, using standing sedimentation 0.5 hour, obtain supernatant and sediment calcium carbonate;(3)Gained supernatant is first passed through into disk centrifugal separator centrifugation to be cleaned Processing, wherein rotating speed are 4000 revs/min;It is directly used as digesting returning for latting drown process in algin production after removal of impurities is handled With water, the wherein salt content of recycle-water is 0.43%, and German degree is 2.8.Gained sediment calcium carbonate is added to pH after collection In 1.5 4700ml waste acid waters, to add 30% hydrochloric acid 800ml, being stirred well to calcium carbonate and react completely, reaction obtains dense Spend for 12.2% calcium chloride solution, hydrochloric acid is then added in the calcium chloride solution of gained causes calcium chloride mass concentration to be at least up to To 12%;(4)After the calcium chloride solution that gained mass concentration is 12.2% is filtered by 300 mesh nets, brown alga is directly used in Glue calcification process in glue production.
Embodiment 3
The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production, comprises the following steps:(1) Removed, obtained by the suspension containing low molecule calcium alginate is derived from the 500L waste Ca waters in algin workshop using air soluble method air supporting To supernatant liquid;Wherein the German degree of waste Ca water is 85, salt content 0.82%;(2)By step(1)Useless calcium after processing The sodium carbonate 965g that 1.2 times of calcium ion moles are added in water carries out decalcification processing.Then settled, using standing sedimentation 0.5 hour, obtain supernatant and sediment calcium carbonate;(3)Gained supernatant is first passed through into disk centrifugal separator centrifugation to be cleaned Processing, wherein rotating speed are 4000 revs/min;It is directly used as digesting returning for latting drown process in algin production after removal of impurities is handled With water, the wherein salt content of recycle-water is 0.80%, and German degree is 1.7.Gained sediment calcium carbonate is added to pH after collection In 1.4 6400ml waste acid waters, to add 31% hydrochloric acid 1100ml, being stirred well to calcium carbonate and react completely, reaction obtains dense Spend for 12.1% calcium chloride solution, hydrochloric acid is then added in the calcium chloride solution of gained causes calcium chloride mass concentration to be at least up to To 12%;(4)After the calcium chloride solution that gained mass concentration is 12.2% is filtered by 300 mesh nets, brown alga is directly used in Glue calcification process in glue production.

Claims (8)

1. the integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production, comprises the following steps:
(1)Suspension containing low molecule calcium alginate in waste Ca water is removed;
(2)By step(1)Decalcifying agent is added in waste Ca water after processing and carries out decalcification processing, is then settled, obtained Supernatant and sediment calcium carbonate;
(3)Gained supernatant is first passed through to the recycle-water for being directly used as that latting drown process is digested in algin production after removal of impurities is handled; Gained sediment calcium carbonate is added into waste acid water after collection, reaction obtains calcium chloride solution, then in the chlorination of gained Hydrochloric acid is added in calcium solution causes calcium chloride mass concentration to be at least up to 12%;Wherein the salt content of recycle-water is less than or equal to 3%;
(4)By gained mass concentration be at least 12% calcium chloride solution filtered after, be directly used in algin production in glue Calcification process.
2. the integrated conduct method of waste Ca water and spent acid water circulation use in algin production according to claim 1, it is special Sign is, the step(1)The suspension containing low molecule calcium alginate in waste Ca water is removed using air floatation machine or centrifuge.
3. the integrated conduct method of waste Ca water and spent acid water circulation use in algin production according to claim 1, it is special Sign is, the step(2)Middle decalcifying agent is sodium carbonate.
4. the integrated conduct method of waste Ca water and spent acid water circulation use in algin production according to claim 1, it is special Sign is, the step(2)The addition of middle decalcifying agent is 1~1.2 times of calcium ion mole in waste Ca water.
5. the integrated conduct method of waste Ca water and spent acid water circulation use in algin production according to claim 1, it is special Sign is, the step(2)Middle sedimentation uses standing sedimentation 0.5~1 hour.
6. the integrated conduct method of waste Ca water and spent acid water circulation use in algin production according to claim 1, it is special Sign is, the step(2)Middle sedimentation carries out continuous sedimentation using inclined plate sedimentation pond.
7. the integrated conduct method of waste Ca water and spent acid water circulation use in algin production according to claim 1, it is special Sign is, the step(3)Middle supernatant carries out removal of impurities processing by 300 mesh net filtrations or centrifuge.
8. the integrated conduct method of waste Ca water and spent acid water circulation use in algin production according to claim 1, it is special Sign is, the step(4)The calcium chloride solution that middle mass concentration is at least 12% is filtered by 300 mesh nets.
CN201510840391.2A 2015-11-27 2015-11-27 The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production Active CN105481136B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510840391.2A CN105481136B (en) 2015-11-27 2015-11-27 The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510840391.2A CN105481136B (en) 2015-11-27 2015-11-27 The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production

Publications (2)

Publication Number Publication Date
CN105481136A CN105481136A (en) 2016-04-13
CN105481136B true CN105481136B (en) 2017-11-10

Family

ID=55668470

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510840391.2A Active CN105481136B (en) 2015-11-27 2015-11-27 The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production

Country Status (1)

Country Link
CN (1) CN105481136B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106674373B (en) * 2016-12-14 2019-09-13 青岛明月海藻集团有限公司 A kind of extracting method and waste Ca water reuse method of alginate
CN109368897A (en) * 2018-10-31 2019-02-22 华北电力大学(保定) A kind of milk of lime process recycles the system and application method of calcium ions and magnesium ions in desulfurization wastewater

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100500597C (en) * 2006-09-21 2009-06-17 寻山集团有限公司 Zero-discharge process for treating, circulating and reutilizing algin production waste water
CN101870528B (en) * 2010-05-27 2011-11-02 中国水产科学研究院黄海水产研究所 Dibasic precipitation method for treating calcium-containing wastewater in phaeophyceae industry
CN103665184B (en) * 2013-12-23 2015-08-19 山东洁晶集团股份有限公司 A kind of method reducing hydrochloric acid calcium chloride consumption in sodium alginate production

Also Published As

Publication number Publication date
CN105481136A (en) 2016-04-13

Similar Documents

Publication Publication Date Title
CA3007906C (en) Process for producing a phosphorus product from wastewater
CN108658345B (en) Method and system for refining salt from high-salt wastewater
CN109439908B (en) Preparation method for preparing high-purity copper powder and recycling crystalline aluminum chloride by using waste etching solution containing copper chloride
CN102674593A (en) Method for treating waste water generated in ionic rare earth production
US10358355B2 (en) Aluminum hydroxide coagulant recovery from water/wastewater treatment sludge
CN108862729A (en) A kind of method of chlor-alkali salt sludge sub-prime recycling comprehensive utilization
CN105481136B (en) The integrated conduct method of waste Ca water and spent acid water circulation use in a kind of algin production
CN109133459A (en) A kind of desulfurization wastewater recycling processing method
JP5118572B2 (en) Sewage treatment method
CN105906129A (en) Method for reutilization of water resources and transformation and utilization of salt in waste water
CN104803560A (en) Method for manufacturing precipitated lignin from production waste water of man-made fiber boards
CN109485189A (en) Ca in high concentration chaff interferent waste water2+And SO42-Intermediate processing
CN104129838A (en) Settlement method of vanadium mud in leached vanadium liquid
CN103896457A (en) Fine chemical wastewater treatment process
CN111547886A (en) Coal mine wastewater recycling comprehensive treatment system
CN102942274B (en) Treatment method of saline and alkaline wastewater in copper oxide production process
CN108486199A (en) Water-soluble chelator, preparation method and the process for treating heavy-metal waste water with it
CN101638242A (en) Method for utilizing barium slag to prepare precipitated barium sulfate and hydrochloric acid
CN106219643A (en) A kind of concentration cycles utilizes the method for industry high-salt wastewater
CN205917092U (en) Sodium alginate waste water processing system
CN105254100A (en) System and method for treating sewage containing salt
CN206298470U (en) A kind of zero-emission equipment of desulfurization wastewater
CN204803207U (en) Professional equipment of materialization mud washing resourceful treatment technology
CN109354331A (en) A kind of method of biologic packing material anaerobic technique processing industrial wastewater
CN104230045B (en) A kind of high salt contains the separation method of sodium-chlor and glycerine in Glycerol Wastewater

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: A Comprehensive Treatment Method for Recycling of Waste Calcium Water and Waste Acid Water in the Production of Alginate

Effective date of registration: 20230428

Granted publication date: 20171110

Pledgee: Rizhao Bank Co.,Ltd. Donggang sub branch

Pledgor: SHANDONG JIEJING Group Corp.

Registration number: Y2023980039602