1271 W Cerritos Ave UNIT 82, Anaheim, CA 92802 • (415)7175155
Stanton, CA
Los Angeles, CA
Orange, CA
810 N Loara St APT B213, Anaheim, CA 92801 • (949)5523712
License Records
Chong H Chang
License #:
2705054029 - Active
Category:
Contractor
Issued Date:
Jan 10, 2000
Expiration Date:
Jan 31, 2018
Type:
Class C
Name / Title
Company / Classification
Phones & Addresses
Chong Chang Owner
Chun Ju Han Il Kwan Korean Restaurant Eating Place
3450 W 6 St, Los Angeles, CA 90020 (213)4801799
Chong Chang Principal
Flamingo Fashion Ret Family Clothing
7016 Pacific Blvd, Walnut Park, CA 90255
Chong H. Chang Director Of Pharmacy, Manager
Rite Aid Drug Palace, Inc Drug Storesprop Strs · Pharmacies & Drug Stores
2060 S Hacienda Blvd, Whittier, CA 91745 2060 S Hacienda Blvd, Hacienda Heights, CA 91745 (626)3335642, (626)9619183
Chong Chang Assistant Vice Presi
Gateway One Lending & Finance Automotive · Indirect Consumer Automobile Financing And Loan Servicing · Indirect Consumer Automobile Finance · Misc Business Credit Institutions
160 N Riverview Dr SUITE 100, Anaheim, CA 92808 Attn Paul Choi 160 N Riverview Dr STE 100, Anaheim, CA 92808 5400 Big Tyler Rd, Charleston, WV 25313 124 W Capitol Ave SUITE 1900, Little Rock, AR 72201 (714)6304653, (714)9213260, (714)7871200
Chong Duk Chang President
Booltina, Inc
830 S Hl St, Los Angeles, CA 90014
Chong C. Chang Owner
Norwalk Lube General Auto Repair
12556 Rosecrans Ave, Norwalk, CA 90650 (562)8021776
There is provided in accordance with the practice of this invention a process for separating albumin from an impure protein fraction containing albumin. Contaminants, in an aqueous solution of the impure protein fraction containing albumin, are precipitated from the solution at a pH of from about 4. 5 to about 4. 7. Additional contaminants that remain soluble are bound to an anion-exchange resin. After the precipitated and anion-exchange-bound contaminants are removed from the albumin-containing solution, the pH of the solution is adjusted to from about 4. 7 to about 6. 1, and additional contaminants are precipitated. Further contaminants are then bound to an anion-exchange resin, and these precipitated and anion-exchange-bound contaminants are removed from the albumin-containing solution.
There is provided in accordance with practice of this invention a process for separating protein fractions from a solution containing proteins and an apparatus for practicing the process. The process and apparatus involve withdrawing from a suspension tank a portion of the suspension contained therein to form a recycle stream. The withdrawn suspension forming the recycle stream contains particles of a selected protein fraction precipitated from a solution containing proteins. Fresh protein solution comprising proteins of the selected protein fraction is mixed into the recycle stream to form a mixed recycle stream. At least a portion of the selected protein fraction proteins in the fresh protein solution precipitate onto previously precipitated selected protein fraction particles suspended in the mixed recycle stream. The mixed recycle stream is introduced back into the suspension tank. A portion of the suspension is withdrawn from the suspension tank in a product stream and precipitated, selected protein fraction particles are recovered from the product stream.
There is provided in accordance with practice of this invention a process for separating protein fractions from a solution containing proteins and an apparatus for practicing the process. The process and apparatus involve withdrawing from a suspension tank a portion of the suspension contained therein to form a recycle stream. The withdrawn suspension forming the recycle stream contains particles of a selected protein fraction precipitated from a solution containing proteins. Fresh protein solution comprising proteins of the selected protein fraction is mixed into the recycle stream to form a mixed recycle stream. At least a portion of the selected protein fraction proteins in the fresh protein solution precipitate onto previously precipitated selected protein fraction particles suspended in the mixed recycle stream. The mixed recycle stream is introduced back into the suspension tank. A portion of the suspension is withdrawn from the suspension tank in a product stream and precipitated, selected protein fraction particles are recovered from the product stream.